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author | hardythe1 | 2014-07-25 12:29:42 +0530 |
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committer | hardythe1 | 2014-07-25 12:29:42 +0530 |
commit | 9dd9b5240afe729a557c6ae683da0b31555a3860 (patch) | |
tree | 8058968e04159f02f98d46dbc664fe12a963b16e /Thermodynamics_by_F_P_Durham/chapter14.ipynb | |
parent | cc0f90b966a13e6edc60165bc4d4d36844af4f2b (diff) | |
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removing unwated
Diffstat (limited to 'Thermodynamics_by_F_P_Durham/chapter14.ipynb')
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diff --git a/Thermodynamics_by_F_P_Durham/chapter14.ipynb b/Thermodynamics_by_F_P_Durham/chapter14.ipynb deleted file mode 100755 index e037e77a..00000000 --- a/Thermodynamics_by_F_P_Durham/chapter14.ipynb +++ /dev/null @@ -1,383 +0,0 @@ -{ - "metadata": { - "name": "", - "signature": "sha256:e1f2ab4731e8126f69d8554acbb321ab940bce50cce33579f99b691416bd49a5" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "Chapter 14: Heat Transfer" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.1, page no. 279" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "T = 50.0 #F\n", - "Q = 3.9 #B/hr-ft^2\n", - "\n", - "#calculation\n", - "#From table 14.1\n", - "k = 0.026 #B/hr-ft-F\n", - "dx = k*T/Q\n", - "\n", - "#result\n", - "print \"Required thickness = ft\", round(dx, 3), \"lb/in^2\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Required thickness = ft 0.333 lb/in^2\n" - ] - } - ], - "prompt_number": 2 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.2, page no. 281" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "x1 = 1.0 #in\n", - "x2 = 4.0 #in\n", - "T1 = 85.0 #F\n", - "T2 = 30.0 #F\n", - "\n", - "#calculation\n", - "QbyA = 12*(T1-T2)/(x1/0.3 + x2/0.026)\n", - "\n", - "#result\n", - "print \"Rate of heat flow = \", round(QbyA, 1), \"B/r-ft^2-F\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Rate of heat flow = 4.2 B/r-ft^2-F\n" - ] - } - ], - "prompt_number": 3 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.3, page no. 283" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "import math\n", - "\n", - "#initialization\n", - "L = 6.5 #in\n", - "thick = 1.0 #in\n", - "k = 0.06 #B/hr-ft-F\n", - "T1 = 350.0 #F\n", - "T2 = 110.0 #F\n", - "\n", - "#calculation\n", - "QbyL = 2*math.pi*k*(T1-T2)/math.log(1+2/L)\n", - "\n", - "#result\n", - "print \"heat flow = %d B/hr-ft\" %QbyL" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "heat flow = 337 B/hr-ft\n" - ] - } - ], - "prompt_number": 4 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.4, page no. 283" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "import math\n", - "\n", - "#initialization\n", - "t = 0.25 #in\n", - "dia = 5.5 #in\n", - "t2 = 0.6 #in\n", - "To = 100.0 #F\n", - "kp = 34.5 #B/hr-ft-F\n", - "ki = 0.05 #B/hr-ft-F\n", - "l = 10.0 #ft\n", - "Q = 2000.0 #B/hr\n", - "\n", - "#calculation\n", - "dT = Q*(1/kp *math.log(1+ 2*t/dia) + 1/ki *math.log(1 + 4*t/(dia+2*t)))/(2*math.pi*l)\n", - "T1 = dT+To\n", - "\n", - "#result\n", - "print \"Inner surface temperature of the pipe = \", round(T1, 1), \"F\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Inner surface temperature of the pipe = 198.2 F\n" - ] - } - ], - "prompt_number": 6 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.5, page no. 286" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "Tsurr = 90.0 #F\n", - "T = 85.0 #F\n", - "\n", - "#calculation\n", - "H = 4.2/(Tsurr-T)\n", - "\n", - "#result\n", - "print \"Film coefficient = %.2f B/hr-ft^2-F\" %H" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Film coefficient = 0.84 B/hr-ft^2-F\n" - ] - } - ], - "prompt_number": 7 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.6, page no. 288" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "k = 0.04 #B/hr-ft-F\n", - "thick = 1.0 #in\n", - "T1 = 90.0 #F\n", - "T2 = 30.0 #F\n", - "Air = 2.5 #B/hr-ft^2-F\n", - "film = 2.0 #B/hr-ft^2-F\n", - "\n", - "#calculation\n", - "U = 1.0/(1.0/Air + thick/12.0/k + 1/film)\n", - "Q = U*(T1-T2)\n", - "\n", - "#result\n", - "print \"Rate of heat transfer per unit square area = %.1f B/hr-ft^2\" %Q" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Rate of heat transfer per unit square area = 20.1 B/hr-ft^2\n" - ] - } - ], - "prompt_number": 8 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.7, page no. 291" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "import math\n", - "\n", - "#initialization\n", - "U = 115.0 #B/hr-ft^2-F\n", - "T1 = 190.0 #F\n", - "T2 = 160.0 #F\n", - "Tc1 = 65.0 #F\n", - "Tc2 = 100.0 #F\n", - "w = 140.0 #lbm/min\n", - "c = 0.8 #B/lbm F\n", - "\n", - "#calculation\n", - "Q = w*60.0*c*(T1-T2) #answer in textbook for Q is wrong. Hence, the difference in final answer\n", - "dT = ((T1-Tc2) - (T2-Tc1))/math.log((T1-Tc2)/(T2-Tc1))\n", - "A = Q/(U*dT)\n", - "\n", - "#result\n", - "print \"Required Area = %.1f ft^2\" %A" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Required Area = 19.0 ft^2\n" - ] - } - ], - "prompt_number": 14 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.8, page no. 294" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "e = 0.8\n", - "T1 = 100+460.0 #R\n", - "T2 = 300+460.0 #R\n", - "\n", - "#calculation\n", - "Qdot = 0.173*10**-8 *(T2**4 - T1**4)/(1/e +1/e -1)\n", - "\n", - "#result\n", - "print \"Radiant heat transfer per sq. foot = %d B/hr-ft^2\" %(Qdot+1)" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Radiant heat transfer per sq. foot = 272 B/hr-ft^2\n" - ] - } - ], - "prompt_number": 15 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example 14.9, page no. 294" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "#initialization\n", - "T1 = 400+460.0 #R\n", - "A = 40.0 #in^2\n", - "e = 0.1\n", - "T2 = 70+460.0 #R\n", - "\n", - "#calculation\n", - "Q = A*e*0.173*10**-8 *(T1**4 - T2**4)/144.0\n", - "\n", - "#result\n", - "print \"Rate of heat transfer = %.2f B/hr\" %Q\n", - "#answer in the book is wrong" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Rate of heat transfer = 22.49 B/hr\n" - ] - } - ], - "prompt_number": 19 - } - ], - "metadata": {} - } - ] -}
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