From 02f1647776a7f366ec75f79547edaecbcff4c028 Mon Sep 17 00:00:00 2001
From: Trupti Kini
Date: Thu, 17 Dec 2015 23:30:18 +0600
Subject: Added(A)/Deleted(D) following books R
_A_Textbook_Of_Engineering_Physics/Chapter11.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter11.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter11_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter11_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter12.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter12.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter12_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter12_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter13.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter13.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter13_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter13_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter14.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter14.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter14_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter14_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter15.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter15.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter15_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter15_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter16.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter16.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter16_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter16_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter17.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter17.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter17_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter17_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter18.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter18.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter18_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter18_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter19.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter19.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter19_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter19_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter21.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter21.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter21_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter21_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter22.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter22.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter22_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter22_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter23.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter23.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter23_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter23_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter24.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter24.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter24_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter24_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter4.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter4.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter4_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter4_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter5.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter5.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter5_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter5_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter6.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter6.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter6_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter6_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter7.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter7.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter7_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter7_1.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter8.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter8.ipynb R
_A_Textbook_Of_Engineering_Physics/Chapter8_1.ipynb ->
A_Textbook_Of_Engineering_Physics/Chapter8_1.ipynb R
_A_Textbook_Of_Engineering_Physics/README.txt ->
A_Textbook_Of_Engineering_Physics/README.txt R
_A_Textbook_Of_Engineering_Physics/screenshots/Chapter11.png ->
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_A_Textbook_Of_Engineering_Physics/screenshots/Chapter11_1.png ->
A_Textbook_Of_Engineering_Physics/screenshots/Chapter11_1.png R
_A_Textbook_Of_Engineering_Physics/screenshots/Chapter12.png ->
A_Textbook_Of_Engineering_Physics/screenshots/Chapter12.png R
_A_Textbook_Of_Engineering_Physics/screenshots/Chapter12_1.png ->
A_Textbook_Of_Engineering_Physics/screenshots/Chapter12_1.png R
_A_Textbook_Of_Engineering_Physics/screenshots/Chapter13.png ->
A_Textbook_Of_Engineering_Physics/screenshots/Chapter13.png R
_A_Textbook_Of_Engineering_Physics/screenshots/Chapter13_1.png ->
A_Textbook_Of_Engineering_Physics/screenshots/Chapter13_1.png D
About_Mumbai_by_sd/hemla.ipynb D About_Mumbai_by_sd/screenshots/warning.png
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About_Mumbai_by_sd/screenshots/warning_2.png R
_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorbption.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorbption.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorption.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer_1.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution_1.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion_1.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species_1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer_.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer_.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer__1.ipynb
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_Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer.ipynb
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Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer_1.ipynb
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_Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/README.txt
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Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/README.txt
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_Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1.ipynb
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Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1.ipynb
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_Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch10.ipynb
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_Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch11.ipynb
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_Theory_Of_Machines/Chapter1.ipynb D _Theory_Of_Machines/Chapter5.ipynb D
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abcd_by_cbvbv/Chapter1.ipynb D abcd_by_cbvbv/Chapter1_1.ipynb D
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-{
- "metadata": {
- "name": ""
- },
- "nbformat": 3,
- "nbformat_minor": 0,
- "worksheets": [
- {
- "cells": [
- {
- "cell_type": "heading",
- "level": 1,
- "metadata": {},
- "source": [
- "Chapter 3 : The mechanical equivalent of heat"
- ]
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.1 pageno : 44"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables\n",
- "m = 20;\t\t\t#calorimeter of water equivalent in gm\n",
- "n = 1030;\t\t\t#weight of water in gm\n",
- "p = 2;\t\t\t#no.of paddles\n",
- "a = 10;\t\t\t#weight of each paddle in kg\n",
- "s = 80;\t\t\t#dismath.tance between paddles in m\n",
- "g = 980;\t\t\t#accelaration due to gravity in cm/sec**2\n",
- "\n",
- "# Calculations\n",
- "E = (p*a*1000*g*s*100);\t\t\t#potential energy in dyne cm\n",
- "T = (E)/(1050*4.18*10**7);\t\t\t#rise in temperature in deg.C\n",
- "\n",
- "# Result\n",
- "print 'the rise in temperature of water is %3.2f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in temperature of water is 3.57 deg.C\n"
- ]
- }
- ],
- "prompt_number": 1
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.2 pageno : 45"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables\n",
- "cp = 0.1;\t\t\t#specific heat of copper in kj/kg-K\n",
- "w = 120;\t\t\t#weight of copper calorimeter in gm\n",
- "a = 1400;\t\t\t#weight of paraffin oil in gm\n",
- "cp1 = 0.6;\t\t\t#specific of parafin oil in kj/kg-K\n",
- "b = 10**8;\t\t\t#force to rotate the paddle in dynes\n",
- "T = 16;\t\t\t#rise in temperature in deg.C\n",
- "n = 900;\t\t\t#no.of revolutions stirred \n",
- "pi = 3.14;\t\t\t#value of pi\n",
- "\n",
- "# Calculations\n",
- "c = 2*pi*b;\t\t\t#work done by a rotating paddle per rotation in dyne cm per rotation\n",
- "d = c*n;\t\t\t#total work done in dyne cm \n",
- "hc = w*cp*16;\t\t\t#heat gained by calorimeter in calories\n",
- "hp = a*cp1*16;\t\t\t#heat gaained by paraffin oil in calories \n",
- "J = d/(hc+hp);\t\t\t#mecanical equivalent of heat in erg/cal\n",
- "\n",
- "# Result\n",
- "print 'mecanical equivalent of heat is %.2e erg/cal'%(J)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "mecanical equivalent of heat is 4.15e+07 erg/cal\n"
- ]
- }
- ],
- "prompt_number": 2
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.3 pageno : 45"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "cp = 0.12;\t\t\t#specific heat of iron in kj/kg-K\n",
- "m = 25;\t\t\t#mass of iron in lb\n",
- "h = 0.4;\t\t\t#horse power developed in 3 min\n",
- "t = 3;\t\t\t#time taken to develop the horse power in min\n",
- "T = 17;\t\t\t#raise in temp in deg.C\n",
- "\n",
- "# Calculations\n",
- "w = h*33000*t;\t\t\t#total work done in ft-lb\n",
- "H = m*cp*T;\t\t\t#aount of heat developed in B.Th.U\n",
- "J = (w)/H;\t\t\t#the value of mechanical equivalent of heat\n",
- "\n",
- "# Result\n",
- "print 'the mechanical equivalent of water is %3.1f ft-lb/B.Th.U'%(J)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mechanical equivalent of water is 776.5 ft-lb/B.Th.U\n"
- ]
- }
- ],
- "prompt_number": 3
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.4 pageno : 45"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "n = 2.;\t\t\t#no.of lead blocks\n",
- "m = 210.;\t\t\t#mass of each lead block in gm\n",
- "v = 20000.;\t\t\t#velocity of block relative to earth in cm/sec\n",
- "J = 4.2*10**7;\t\t\t#mechanical equivalent of heat in ergs/calorie\n",
- "cp = 0.03;\t\t\t#specific heat of lead in kj/kg-K\n",
- "\n",
- "# Calculations\n",
- "E = (m*v**2)/2;\t\t\t#kinetic energy of each block in ergs\n",
- "E2 = n*E;\t\t\t#total kinetic energy in ergs\n",
- "T = E2/(J*m*n*cp);\t\t\t#mean rise in temperature in T\n",
- "\n",
- "# Result\n",
- "print 'the mean rise in temperature is %3.1f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mean rise in temperature is 158.7 deg.C\n"
- ]
- }
- ],
- "prompt_number": 4
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.5 pageno : 45"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "h = 150;\t\t\t#height froom which ball fallen in ft\n",
- "cp = 0.03;\t\t\t#specific heat of lead in kj/kg-K\n",
- "J = 778;\t\t\t#mechanical equivalent of heat in ft lb/B.Th.U\n",
- "\n",
- "# Calculations\n",
- "#work done in falling is equal to heat absorbed by the ball\n",
- "T = 160./(J*cp)*(5./9);\t\t\t#the raise in temperature in T\n",
- "\n",
- "# Result\n",
- "print 'the raise in temperature is %3.1f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the raise in temperature is 3.8 deg.C\n"
- ]
- }
- ],
- "prompt_number": 5
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.6 pageno : 46"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "import math \n",
- "# Variables \n",
- "w = 26.6;\t\t\t#work done one horse in to raise the temperature in lb\n",
- "T1 = 32.;\t\t\t#temperature at initial in deg.F\n",
- "T2 = 212.;\t\t\t#temperature at final in deg.F\n",
- "t = 2.5;\t\t\t#time to raise the tmperature in hrs\n",
- "p = 25.;\t\t\t#percentage of heat lossed \n",
- "\n",
- "# Calculations\n",
- "#only 75% of heat is utillised\n",
- "x = w*180.*100.*778./((100-p)*150);\t\t\t#the rate at which horse worked\n",
- "\n",
- "# Result\n",
- "print 'the rate at which horse worked is %3.0f ft-lb wt/min'%(x)\n",
- "print \"Note : Answer in book is rounded off, Please calculate manually. This answer is accurate.\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rate at which horse worked is 33112 ft-lb wt/min\n",
- "Note : Answer in book is rounded off, Please calculate manually. This answer is accurate.\n"
- ]
- }
- ],
- "prompt_number": 7
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.7 pageno : 46"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "l = 100.;\t\t\t#length of glass tube in cm\n",
- "m = 500.;\t\t\t#mass of mercury in glass tube in gm\n",
- "n = 20.;\t\t\t#number of times inverted i succession\n",
- "cp = 0.03;\t\t\t#specific heat of mercury in cal/gm/deg.C\n",
- "J = 4.2;\t\t\t#joule's equivalent in j/cal\n",
- "g = 981.;\t\t\t#accelaration due to gravity in cm/s**2\n",
- "\n",
- "# Calculations\n",
- "PE = m*g*l;\t\t\t#potential energy for each time in ergs\n",
- "TE = PE*n;\t\t\t#total loss in ergs\n",
- "T = TE/(m*cp*J*10**7);\t\t\t#rise in temperature in deg.C\n",
- "#if T is the rise in temperature,then heat devoloped is m*cp*T\n",
- "\n",
- "# Result\n",
- "print 'the rise in temperature is %3.2f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in temperature is 1.56 deg.C\n"
- ]
- }
- ],
- "prompt_number": 8
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.8 page no : 46"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "\n",
- "# Variables \n",
- "d = 0.02;\t\t\t#diameter of the copper wire in cm\n",
- "i = 1;\t\t\t#current in amp\n",
- "T = 100;\t\t\t#maximum steady temperature in deg.C\n",
- "r = 2.1;\t\t\t#resistance of the wire in ohm cm\n",
- "J = 4.2;\t\t\t#mechanical equivalent of heat in j/cal\n",
- "a = 3.14*d**2/4;\t\t\t#area of the copper wire in sq.cm\n",
- "a2 = 1;\t\t\t#area of the copper surface in sq.cm\n",
- "\n",
- "# Calculations \n",
- "l = 1/(2*3.14*d/2);\t\t\t#length corresponding to the area in cm\n",
- "R = r*l/a;\t\t\t#resistance of the copper wire in ohm\n",
- "w = R*a2**2;\t\t\t#work done in joule\n",
- "h = w/J;\t\t\t#heat devoleped in cal\n",
- "\n",
- "# Result\n",
- "print 'the heat developed is %.f calories'%(round(h,-1))\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the heat developed is 25360 calories\n"
- ]
- }
- ],
- "prompt_number": 11
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.9 pageno: 47"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "import math \n",
- "\n",
- "# Variables\n",
- "h = 10000;\t\t\t#vertical height of water fall in cm\n",
- "v = 5;\t\t\t #volume disharged per sec in litres\n",
- "J = 4.18;\t\t\t#joule's constant in j/cal\n",
- "g = 981;\t\t\t#accelaration due to gravity in cm/sec**2\n",
- "\n",
- "# Calculations\n",
- "m = v*1000;\t\t\t#mass of water disharged per sec in gm\n",
- "w = m*h*g;\t\t\t#work done in falling through 100m in erg\n",
- "H = (v*10**7 *g)/(J*10**7);\t#quantity of heat produced in cal\n",
- "T = H/m;\t\t\t#rise in temperature in deg.C\n",
- "\n",
- "# Result\n",
- "print 'the quantity of heat produced is %3f cal \\\n",
- "\\nthe rise in temperature is %3.2f deg.C'%(H,T)\n",
- "\n",
- "print \"Note : Answer for part A in book is wrong. Please calculate manually.\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the quantity of heat produced is 1173.444976 cal \n",
- "the rise in temperature is 0.23 deg.C\n",
- "Note : Answer for part A in book is wrong. Please calculate manually.\n"
- ]
- }
- ],
- "prompt_number": 15
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.10 page no : 47"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "\n",
- "# Variables \n",
- "cp = 0.03;\t\t\t#specific heat of lead in kj/kg.k\n",
- "v = 10000;\t\t\t#initial velocity of bullet in cm/sec\n",
- "J = 4.2*10**7;\t\t\t#joules constant in ergs/cal\n",
- "\n",
- "# Calculations\n",
- "ke = (v**2)/2;\t\t\t#kinetic energy of the bullet per unit mass in (cm/sec)**2\n",
- "T = ke*95/(cp*J*100);\t\t\t#rise in temperature in deg.C\n",
- "\n",
- "# Result\n",
- "print 'the rise in temperature is %3.1f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in temperature is 37.7 deg.C\n"
- ]
- }
- ],
- "prompt_number": 16
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.11 page no : 47"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "h = 5000.;\t\t\t#height of the niagara falls in cm\n",
- "J = 4.2*10**7;\t\t#joules constant in ergs per cal\n",
- "g = 981;\t\t\t#accelaration due to gravity in cm/sec**2\n",
- "\n",
- "#CALCULATIONS\n",
- "w = h*g;\t\t\t#work done per unit mass in ergs/gn\n",
- "T = w/J;\t\t\t#rise in temperature in deg.C\n",
- "\n",
- "# Result\n",
- "print 'the rise in temperature is %3.2f deg.C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in temperature is 0.12 deg.C\n"
- ]
- }
- ],
- "prompt_number": 17
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.12 page no : 48\n"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "import math \n",
- "\n",
- "# Variables \n",
- "E1 = 3.75;\t\t\t#potential difference in v\n",
- "E2 = 3.;\t\t\t#potential differnce in v\n",
- "i1 = 2.5;\t\t\t#current in amp\n",
- "i2 = 2;\t\t\t #current in amp\n",
- "T = 2.7;\t\t\t#the rise in temperature of the water in deg.C\n",
- "m1 = 48.;\t\t\t#water flow rate at 3 volts in gm/min\n",
- "m2 = 30.;\t\t\t#water flow rate at 3.75volts in gm/min\n",
- "s = 1;\t\t\t #specific heat of the water kj/kg-K\n",
- "\n",
- "# Calculations\n",
- "J = (E1*i1-E2*i2)/(s*T*(m1-m2)/60);\t\t\t#the mechanical equivalent in j/cal\n",
- "\n",
- "# Result\n",
- "print 'the mechanical equivalent is %3.3f j/cal'%(J)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mechanical equivalent is 4.167 j/cal\n"
- ]
- }
- ],
- "prompt_number": 18
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.13 page no : 48"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "\n",
- "# Variables \n",
- "R = 64*10**7;\t\t\t#mean radius of the earth in cm\n",
- "cp = 0.15;\t\t\t#specific heat of earth in kj/kg-K\n",
- "J = 4.2*10**7;\t\t\t#joules consmath.tant in erg/cal\n",
- "\n",
- "# Calculations\n",
- "i = 2./5*R**2;\t\t\t#moment of inertia of the earth per unit mass in joules\n",
- "w = (2*3.14)/(24*60*60);\t\t\t#angular velocity of the earth in rad/sec\n",
- "T = (i*w**2)/(2*J*cp);\t\t\t#rise in temperature in deg.C\n",
- "\n",
- "# Result\n",
- "print 'the rise in the temperature is %.1f deg C'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in the temperature is 68.7 deg C\n"
- ]
- }
- ],
- "prompt_number": 6
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.14 page no : 49"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "cp = 1.25;\t\t\t#specific heat of helium inkj/kg-K\n",
- "v = 1000;\t\t\t#volume of the gas in ml\n",
- "w = 0.1785;\t\t\t#mass of the gas at N.T.P in gm\n",
- "p = 76*13.6*981;\t#pressure of the gas at N.T.P in dynes\n",
- "T = 273;\t\t\t#temperature at N.T.P in K\n",
- "\n",
- "# Calculations\n",
- "V = 1000/w;\t\t\t#volume occupied by the 1gm of helium gas in cc\n",
- "cv = cp/1.66;\t\t#specific heat at constant volume it is monatomuc gas kj/kg-K\n",
- "r = p*V/T;\t\t\t#gas constant in cm**3.atm./K.mol\n",
- "J = r/(cp-cv);\t\t#mechanical equivalent of heat in erg/cal\n",
- "\n",
- "# Result\n",
- "print 'the mechanical equivalent of heat is %.2e ergs/calories'%(J)\n",
- "print \"Note: answer slightly different because of rounding error.\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mechanical equivalent of heat is 4.19e+07 ergs/calories\n",
- "Note: answer slightly different because of rounding error.\n"
- ]
- }
- ],
- "prompt_number": 20
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "\n",
- "Example 3.15 pageno : 49"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables \n",
- "n = 1./273; \t\t\t#coefficent of expaaansion of air\n",
- "a = 0.001293;\t \t\t#density of air in gm/cc\n",
- "cp = 0.2389;\t\t \t#specific heat at consmath.tant pressure in kj/kg.K\n",
- "p = 76*13.6*981;\t\t\t#pressure at 0 deg.C in dynes\n",
- "\n",
- "# Calculations\n",
- "J = (p*n)/(a*(cp-(cp/1.405)));\t\t\t#mechanical equivalent of heat\n",
- "\n",
- "# Result\n",
- "print 'mechanical equivalent of heat is %.2e ergs/cal'%(J)\n",
- "print \"Note: answer slightly different because of rounding error.\"\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "mechanical equivalent of heat is 4.17e+07 ergs/cal\n",
- "Note: answer slightly different because of rounding error.\n"
- ]
- }
- ],
- "prompt_number": 22
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.16 pageno : 49"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "import math \n",
- "# Variables \n",
- "r = 120./60;\t\t\t#rate of flow of water in gm/sec\n",
- "T1 = 27.30;\t\t\t#temperature at initial in deg.C\n",
- "T2 = 33.75;\t\t\t#temperature at final in deg.C\n",
- "v = 12.64;\t\t\t#potential drop in volts\n",
- "s = 1.; \t\t\t#specific heat of water in kj/kg-K\n",
- "i = 4.35;\t\t\t#current through the heating element in amp\n",
- "\n",
- "# Calculations\n",
- "J = (v*i)/(r*s*(T2-T1));\t\t\t#the mechanical equivalent of heat in joule/calorie\n",
- "\n",
- "# Result\n",
- "print 'the mechanical equivalent of heat is %3.2f j/cal'%(J)\n",
- "print \"Note: answer slightly different because of rounding error.\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mechanical equivalent of heat is 4.26 j/cal\n",
- "Note: answer slightly different because of rounding error.\n"
- ]
- }
- ],
- "prompt_number": 24
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.17 page no : 50"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "\n",
- "# Variables \n",
- "cp = 6.865;\t\t\t#molar specific heat of hydrogen at consmath.tant pressure in kj/kg-K\n",
- "cv = 4.880;\t\t\t#molar specific heat of hydrogen at consmath.tant volume in kj/kg-K\n",
- "p = 1.013*10**6;\t\t\t#atmospheric pressure in dynes/cm**2\n",
- "v = 22.4*10**3;\t\t\t#gram molar volume in ml\n",
- "T = 273;\t\t\t#temperature at N.T.P in kelvins\n",
- "\n",
- "# Calculations\n",
- "J = (p*v)/(T*(cp-cv));\t\t\t#mechanical equivalent of heat\n",
- "\n",
- "# Result\n",
- "print 'the mechanical equivalent of heat is %.2e ergs/cal'%(J)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the mechanical equivalent of heat is 4.19e+07 ergs/cal\n"
- ]
- }
- ],
- "prompt_number": 26
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.18 page no : 50"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "import math \n",
- "# Variables\n",
- "v = 1000.;\t\t\t#volume of hydrogen in ml\n",
- "t = 273.;\t\t\t#tempature of hydrogen in kelvin\n",
- "p = 76.;\t\t\t#pressure of hydrogen in mm of hg\n",
- "w = 0.0896;\t\t\t#weigh of hydrogen in gm\n",
- "cp = 3.409;\t\t\t#specific heat of hydogen in kj/kg-K\n",
- "cv = 2.411;\t\t\t#specific heat of hydrogen in kj/kg-K\n",
- "g = 981.;\t\t\t#accelaration due to gravity in cm/sec**2\n",
- "a = 13.6;\t\t\t#density of mercury in gm/cm**2\n",
- "\n",
- "# Calculations\n",
- "J = (p*v*g*a)/(w*t*(cp-cv));\t\t\t#mechanical equivalent of heat in ergs/cals\n",
- "\n",
- "# Result\n",
- "print 'mechanical equivalent of heat is %.2e ergs/calorie'%(J)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "mechanical equivalent of heat is 4.15e+07 ergs/calorie\n"
- ]
- }
- ],
- "prompt_number": 1
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.19 page no : 50"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables\n",
- "cp = 0.23;\t\t\t#specific heat at constant pressure in kj/kg-K\n",
- "a = 1.18;\t\t\t#density of air in gm/lit\n",
- "J = 4.2*10**7;\t\t\t#mechanical equivalent of heat in ergs/cal\n",
- "t = 300;\t\t\t#temperature of air in kelvin\n",
- "p = 73*13.6*981;\t\t\t#pressure of air in dynes\n",
- "\t\t\t#cp-cv = (r/J) = pv/(tj)\n",
- "\n",
- "#CALCULATON\n",
- "cv = cp-(p*1000/(a*t*J));\t\t\t#specific heat at constant volume in calories\n",
- "\n",
- "# Result\n",
- "print 'the specific heat at constant volume is %.4f calories'%(cv)\n",
- "print \"Note: answer slightly different because of rounding error.\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the specific heat at constant volume is 0.1645 calories\n",
- "Note: answer slightly different because of rounding error.\n"
- ]
- }
- ],
- "prompt_number": 29
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.20 pageno : 51"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables\n",
- "t1 = 0;\t\t\t#temperature of water in deg.C\n",
- "t2 = 0;\t\t\t#temperature of ice in deg.C\n",
- "J = 4.18*10**7;\t\t\t#the joules thomson coefficent in erg/cal\n",
- "l = 80;\t\t\t#latent heat og fusion kj/kg\n",
- "g = 981;\t\t\t#accelaration due to gravity in cm/sec**2\n",
- " \n",
- "# Calculations\n",
- "h = l*J/(15*g);\t\t\t#height from which ice has fallen\n",
- "\n",
- "# Result\n",
- "print 'the height from which ice has fallen is %.2e cm'%(h)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the height from which ice has fallen is 2.27e+05 cm\n"
- ]
- }
- ],
- "prompt_number": 30
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.21 page no : 51"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "\n",
- "# Variables\n",
- "T = 80;\t\t\t#temperature of bullet in deg.C\n",
- "cp = 0.03;\t\t\t#specific heat of lead in kj/kg-K\n",
- "J = 4.2;\t\t\t#mechanical equivalent of heat in j/cal\n",
- "\n",
- "# Calculations\n",
- "h = T*cp;\t\t\t#heat developed per unit mass in calorie\n",
- "v = (J*10**7*h*2/0.9)**0.5;\t\t\t#velocity of bullet in cm/sec\n",
- "\n",
- "# Result\n",
- "print 'the velocity of bullet is %.1e cm/sec'%(v)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the velocity of bullet is 1.5e+04 cm/sec\n"
- ]
- }
- ],
- "prompt_number": 31
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Example 3.22 pageno : 51"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "\n",
- "# Variables\n",
- "w = 5.0;\t\t\t#weight of lead ball in lb\n",
- "cp = 0.032;\t\t\t#specific heat of lead in Btu/lbdeg.F\n",
- "h = 50;\t\t\t#height at which ball thrown in feets\n",
- "v = 20;\t\t\t#vertical speed in ft/sec\n",
- "g = 32;\t\t\t#accelararion due to gravity in ft/sec**2\n",
- "\n",
- "# Calculations\n",
- "u = (v**2)+2*g*h\n",
- "ke = (w/2*(u));\t\t\t#kinetic energy of the ball at ground\n",
- "T = ke/(2*32*778*w*cp);\t\t\t#rise of temperature in deg.F\n",
- "\n",
- "# Result\n",
- "print 'the rise in temperature is %.1f deg.F'%(T)\n"
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "the rise in temperature is 1.1 deg.F\n"
- ]
- }
- ],
- "prompt_number": 32
- }
- ],
- "metadata": {}
- }
- ]
-}
\ No newline at end of file
--
cgit