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diff --git a/Heat_Transfer_In_SI_Units_by_J_P_Holman/1-Introduction.ipynb b/Heat_Transfer_In_SI_Units_by_J_P_Holman/1-Introduction.ipynb new file mode 100644 index 0000000..f8b6f63 --- /dev/null +++ b/Heat_Transfer_In_SI_Units_by_J_P_Holman/1-Introduction.ipynb @@ -0,0 +1,237 @@ +{ +"cells": [ + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "# Chapter 1: Introduction" + ] + }, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.1: conduction_through_copper_plate.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.1\n\n\n');\n", +"// conduction through copper plate\n", +"// illustration1.1\n", +"// solution\n", +"\n", +"k = 370; // [W/m] at 250 degree celsius\n", +"dt = 100-400;//[degree celsius] temperature difference\n", +"dx = 3*10^(-2);//[m] thickness of plate\n", +"//calculating heat transfer per unit area from fourier's law\n", +"q = -k*dt/dx;//[MW/square meter]\n", +"printf('rate of heat transfer per unit area is %f MW/square meter',q/1000000);" + ] + } +, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.2: convection_calculation.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.2\n\n\n');\n", +"// convection calculation\n", +"// illustration1.2\n", +"// solution\n", +"\n", +"Twall = 250;//[degree celsius] wall temperature\n", +"Tair = 20;//[degree celsius] air temperature\n", +"h = 25;//[W/square meter] heat transfer coefficient\n", +"l = 75*10^(-2);//[m] length of plate\n", +"b = 50*10^(-2);//[m] width of plate\n", +"area = l*b;//[square meter] area of plate\n", +"dt = 250-20;//[degree celsius]\n", +"// from newton's law of cooling\n", +"q = h*area*dt;// [W]\n", +"printf('rate of heat transfer is %f kW',q/1000);\n", +"" + ] + } +, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.3: multimode_heat_transfer.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.3\n\n\n');\n", +"// multimode heat transfer\n", +"// illustration1.3\n", +"// solution\n", +"\n", +"Qconv = 2156;// [W] from previous problem\n", +"Qrad = 300;// [W] given\n", +"dx = 0.02;// [m] plate thicknesss\n", +"l = 0.75;// [m] length of plate \n", +"w = 0.5;// [m] width of plate\n", +"k = 43;//[W/m] from table 1.1\n", +"area = l*w;//[square meter] area of plate\n", +"Qcond = Qconv+Qrad;// [W]\n", +"dt = Qcond*dx/(k*area);// [degree celsius] temperature difference\n", +"Ti = 250+dt;// inside temperature\n", +"printf('the inside plate temperature is therefore %f degree celsius',Ti);" + ] + } +, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.4: heat_source_and_convection.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.4\n\n\n');\n", +"// heat source and convection\n", +"// illustration1.4\n", +"// solution\n", +"\n", +"d = 1*10^(-3);//[m] diameter of wire\n", +"l = 10*10^(-2);//[m] length of wire\n", +"Sarea = 22*d*l/7;//[square meter] surface area of wire\n", +"h = 5000;//[W/square meter] heat transfer coefficient\n", +"Twall = 114;// [degree celsius]\n", +"Twater = 100;// [degree celsius]\n", +"//total convection loss is given by equation(1-8)\n", +"Q = h*Sarea*(Twall-Twater);// [W]\n", +"printf('heat transfer is therefore %f W',Q);\n", +"printf(' this is equal to the electric power which must be applied');" + ] + } +, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.5: radiation_heat_transfer.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.5\n\n\n');\n", +"// radiation heat transfer\n", +"// illustration1.5\n", +"// solution\n", +"\n", +"sigma = 5.699*10^(-8);//[W/square meter*k^(4)] universal constant\n", +"T1 = 273.15+800;// [k] first plate temperature\n", +"T2 = 273.15+300;// [k] second plate temperature\n", +"//equation(1-10) may be employed for this problem\n", +"Q = sigma*((T1^(4))-(T2^(4)));// [W/square meter]\n", +"printf('heat transfer per unit area is %f kW/square meter',Q/1000);" + ] + } +, +{ + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Example 1.6: total_heat_loss_by_convection_and_radiation.sce" + ] + }, + { +"cell_type": "code", + "execution_count": null, + "metadata": { + "collapsed": true + }, + "outputs": [], +"source": [ +"clear;\n", +"clc;\n", +"printf('\t\t\tExample Number 1.6\n\n\n');\n", +"// total heat loss by convection and radiation\n", +"// illustration1.6\n", +"// solution\n", +"\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", +"Q1 = h*22*d*(Twall-Tair)/7;//[W/m] convection loss per unit length\n", +"sigma = 5.669*10^(-8);// [W/square meter*k^(4)] universal constant\n", +"T1 = 273.15+Twall;// [k]\n", +"T2 = 273.15+Tair;// [k]\n", +"Q2 = emi*22*d*sigma*((T1^(4))-(T2^(4)))/7;// [W/m] heat loss due to radiation per unit length\n", +"Qtotal = Q1+Q2;// [W/m] total heat loss per unit length\n", +"printf('total heat loss is therefore %f W/m',Qtotal);" + ] + } +], +"metadata": { + "kernelspec": { + "display_name": "Scilab", + "language": "scilab", + "name": "scilab" + }, + "language_info": { + "file_extension": ".sce", + "help_links": [ + { + "text": "MetaKernel Magics", + "url": "https://github.com/calysto/metakernel/blob/master/metakernel/magics/README.md" + } + ], + "mimetype": "text/x-octave", + "name": "scilab", + "version": "0.7.1" + } + }, + "nbformat": 4, + "nbformat_minor": 0 +} |