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diff --git a/Heat_Transfer_in_SI_units_by_Holman/Chapter1.ipynb b/Heat_Transfer_in_SI_units_by_Holman/Chapter1.ipynb new file mode 100644 index 00000000..0af0c439 --- /dev/null +++ b/Heat_Transfer_in_SI_units_by_Holman/Chapter1.ipynb @@ -0,0 +1,302 @@ +{ + "cells": [ + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "# Chapter 1 Introduction" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.1" + ] + }, + { + "cell_type": "code", + "execution_count": 7, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Rate of heat transfer per unit area is 3.7 MW/sq meter\n" + ] + } + ], + "source": [ + "#Example Number 1.1\n", + "# HOW MUCH HEAT IS TRANSFERRED THROUGH THE PLATE\n", + "\n", + "#VARIABLE DECLARATION\n", + "\n", + "k = 370 \t\t\t # [W/m] at 250 degree celsius\n", + "dt = 100-400 \t\t\t#[degree celsius] temperature difference\n", + "dx = 3*10**(-2) \t\t#[m] thickness of plate\n", + "\n", + "#CALCULATION\n", + "\n", + "q = -k*dt/dx \t\t\t#[MW/square meter]\n", + "\n", + "#RESULTS\n", + "\n", + "print \"Rate of heat transfer per unit area is\", q/1000000 ,\"MW/sq meter\"\n" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.2" + ] + }, + { + "cell_type": "code", + "execution_count": 2, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Rate of heat transfer is 2.156 kW\n" + ] + } + ], + "source": [ + "#Example Number 1.2\n", + "# CALCULATE THE HEAT TRANSFER\n", + "\n", + "#Variable declaration\n", + "\n", + "Twall = 250 \t\t\t#[degree celsius] wall temperature\n", + "Tair = 20 \t\t\t#[degree celsius] air temperature\n", + "h = 25 \t\t\t\t#[W/square meter] heat transfer coefficient\n", + "l = 75*10**(-2) \t\t#[m] length of plate\n", + "b = 50*10**(-2) \t\t#[m] width of plate\n", + "area = l*b \t\t\t#[square meter] area of plate\n", + "dt = 250-20 \t\t\t#[degree celsius]\n", + "\n", + "\n", + "#Calculation\n", + "\n", + "q = h*area*dt \t\t\t# [W] from newton's law of cooling\n", + "\n", + "\n", + "#Result\n", + "\n", + "print\"Rate of heat transfer is\",round(q/1000,3),\"kW\" \n", + "\n" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.3" + ] + }, + { + "cell_type": "code", + "execution_count": 3, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Inside plate temperature is 253.05 degree C\n" + ] + } + ], + "source": [ + "#Example Number 1.3\n", + "# Calculate the inside plate temperature.\n", + "\n", + "#variable declaration\n", + "\n", + "Qconv = 2156 \t # [W] from previous problem\n", + "Qrad = 300\t\t # [W] given\n", + "dx = 0.02\t\t # [m] plate thicknesss\n", + "l = 0.75 \t\t # [m] length of plate \n", + "w = 0.5 \t\t # [m] width of plate\n", + "k = 43\t\t\t #[W/m] from table 1.1\n", + "area = l*w\t\t #[square meter] area of plate\n", + "\n", + "#Calculation\n", + "\n", + "Qcond = Qconv+Qrad \t # [W]\n", + "dt = Qcond*dx/(k*area) \t # [degree celsius] temperature difference\n", + "Ti = 250+dt \t\t # inside temperature\n", + "\n", + "#Results\n", + "\n", + "print\"Inside plate temperature is\",round(Ti,2),\"degree C\"" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.4" + ] + }, + { + "cell_type": "code", + "execution_count": 4, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Heat transfer is: 22.0 W\n", + " This is equal to the electric power which must be applied\n" + ] + } + ], + "source": [ + "#Example Number 1.4\n", + "# Calculate electric power to be supplied to the wire \n", + "\n", + "#Variable declaration\n", + "\n", + "d = 1*10**(-3) \t\t#[m] diameter of wire\n", + "l = 10*10**(-2) \t#[m] length of wire\n", + "Sarea = 22*d*l/7 \t#[square meter] surface area of wire\n", + "h = 5000 \t\t#[W/square meter] heat transfer coefficient\n", + "Twall = 114 \t\t# [degree celsius]\n", + "Twater = 100\t # [degree celsius]\n", + "\n", + "#total convection loss is given by equation(1-8)\n", + "\n", + "#Calculation\n", + "\n", + "Q = h*Sarea*(Twall-Twater) # [W]\n", + "\n", + "#Results\n", + "\n", + "print\"Heat transfer is:\",Q,\"W\" \n", + "print\" This is equal to the electric power which must be applied\"\n" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.5" + ] + }, + { + "cell_type": "code", + "execution_count": 5, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Heat transfer per unit area is: 69.03 kW/sq meter\n" + ] + } + ], + "source": [ + "#Example Number 1.5\n", + "# radiation heat transfer\n", + "# Calculate the heat transfer per unit area\n", + "\n", + "#Variable declaration\n", + "\n", + "sigma = 5.669*10**(-8) \t\t#[W/square meter*k^(4)] universal constant\n", + "T1 = 273+800 \t\t\t# [k] first plate temperature\n", + "T2 = 273+300 \t\t\t# [k] second plate temperature\n", + "\n", + "#equation(1-10) may be employed for this problem\n", + "\n", + "#Calculation\n", + "Q = sigma*(T1**4-T2**4) \t# [W/square meter]\n", + "\n", + "#Results\n", + "\n", + "print\"Heat transfer per unit area is:\",round(Q/1000,2),\" kW/sq meter\"\n" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Exa 1.6" + ] + }, + { + "cell_type": "code", + "execution_count": 6, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "Total heat loss is: 55.67 W/m\n" + ] + } + ], + "source": [ + "#Example Number 1.6\n", + "# total heat loss by convection and radiation\n", + "\n", + "#Variable declaration\n", + "d = 0.05 #[m] diameter of pipe\n", + "Twall = 50 #[degree celsius] \n", + "Tair = 20 #[degree celsius]\n", + "emi = 0.8 #emissivity\n", + "h = 6.5 #[W/square meter] heat transfer coefficient for free convection\n", + "import math\n", + "Q1 = h*math.pi*d*(Twall-Tair) #[W/m] convection loss per unit length\n", + "sigma = 5.669*10**(-8) # [W/square meter*k^(4)] universal constant\n", + "T1 = 273+Twall # [k]\n", + "T2 = 273+Tair # [k]\n", + "Q2 = emi*math.pi*d*sigma*((T1**(4))-(T2**(4))) # [W/m] heat loss due to radiation per unit length\n", + "Qtotal = Q1+Q2 # [W/m] total heat loss per unit length\n", + "\n", + "print\"Total heat loss is:\",round(Qtotal,2),\"W/m\"\n" + ] + } + ], + "metadata": { + "kernelspec": { + "display_name": "Python 2", + "language": "python", + "name": "python2" + }, + "language_info": { + "codemirror_mode": { + "name": "ipython", + "version": 2 + }, + "file_extension": ".py", + "mimetype": "text/x-python", + "name": "python", + "nbconvert_exporter": "python", + "pygments_lexer": "ipython2", + "version": "2.7.6" + } + }, + "nbformat": 4, + "nbformat_minor": 0 +} |