Added(A)/Deleted(D) following books

M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/README.txt M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter10_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter10_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter11.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter11_1.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter12_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter12_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter13_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter13_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter14_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter14_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter15_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter15_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter16_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter16_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter1_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter1_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter2_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter2_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter3_1.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter4.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter4_1.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter5.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter5_1.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter6_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter6_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter7_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter7_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter8_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter8_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter9_2.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter9_3.ipynb M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_01_00.png M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_01_00_1.png M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_01_25.png M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_01_25_1.png M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_02_44.png M 1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17_02_44_1.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter25_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter25_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter25_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter26_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter26_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter26_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter27_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter27_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter27_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter28_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter28_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter28_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter29_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter29_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter29_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter30_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter30_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter30_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter31_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter31_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter31_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter32_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter32_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter32_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter33_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter33_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter33_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter34_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter34_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter34_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter35_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter35_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter35_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter36_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter36_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter36_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter37_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter37_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter37_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter38_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter38_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter38_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter39_4.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter39_5.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/chapter39_6.ipynb M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example32_4.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example32_5.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example32_6.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example33_4.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example33_5.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter29example33_6.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter32example30_4.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter32example30_5.png M A_Textbook_of_Electrical_Technology_:_AC_and_DC_Machines_(Volume_-_2)_by_A_K_Theraja_B_L_Thereja/screenshots/chapter32example30_6.png M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap10_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap11_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap12_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap13_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap16_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap17_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap18_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap19_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap20_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap21_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap22_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap23_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap24_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap25_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap26_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap27_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap28_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap29_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap30_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap31_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap32_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap33_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap34_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap3_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap5_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap7_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap8_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/Chap9_2.ipynb M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/README.txt M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/screenshots/11DrainCurrentGraph.png M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/screenshots/18VceVsIce.png M A_Textbook_of_Electronic_Circuits_by_R._S._Sedha/screenshots/24GainGraph.png M Analog_Electronics_by_U._A._Bakshi_And_A._P._Godse/README.txt M Applied_Thermodynamics_and_Engineering_by_T._D._Eastop_and_A._Mcconkey/README.txt A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter01.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter02.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter03.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter04.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter05.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter10.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter11.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter12.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter13.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter14.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter15.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter16.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter17.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter18.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter19.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter20.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter21.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter22.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter6.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter7.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter8.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter9.ipynb A Basic_And_Applied_Thermodynamics_by_P._K._Nag/screenshots/16.11.png A Basic_And_Applied_Thermodynamics_by_P._K._Nag/screenshots/3.3.png A Basic_And_Applied_Thermodynamics_by_P._K._Nag/screenshots/7.10.png R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter1.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter1.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter10.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter10.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter13.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter13.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter14.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter14.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter15.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter15.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter2.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter2.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter3.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter3.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter4.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter4.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter5.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter5.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter6.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter6.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter7.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter7.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter8.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter8.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/chapter9.ipynb -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/chapter9.ipynb R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/screenshots/Screenshot_(88).png -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/screenshots/Screenshot_(88).png R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/screenshots/Screenshot_(89).png -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/screenshots/Screenshot_(89).png R Basic_Electronics_(Electronics_Engineering)_by_J.B.Gupta/screenshots/Screenshot_(90).png -> Basic_Electronics_(Electronics_Engineering)_by_J_B_Gupta/screenshots/Screenshot_(90).png M Coulson_And_Richardsons_Chemical_Engineering,_Volume_2_by_J._M._Coulson,_J._F._Richardson,_J._R._Backhurst_And_J._H._Harker/README.txt M Digital_Communications_by_S._Haykin/Chapter1.ipynb M Digital_Communications_by_S._Haykin/Chapter2.ipynb M Digital_Communications_by_S._Haykin/Chapter3.ipynb M Digital_Communications_by_S._Haykin/Chapter4.ipynb M Digital_Communications_by_S._Haykin/Chapter5.ipynb M Digital_Communications_by_S._Haykin/Chapter6.ipynb M Digital_Communications_by_S._Haykin/Chapter7.ipynb M Digital_Communications_by_S._Haykin/Chapter8.ipynb M Digital_Communications_by_S._Haykin/Chapter9.ipynb M Digital_Communications_by_S._Haykin/screenshots/Ch-6_RaisedCosineSpectrum.png M Digital_Communications_by_S._Haykin/screenshots/Ch6_powerSpectralDensities.png M Digital_Communications_by_S._Haykin/screenshots/ch6_sinc_pilse.png M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/README.txt M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter10_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter11_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter12_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter13_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter14_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter15_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter16_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter17_1.ipynb M Electrical_Engineering_-_Principles_And_Applications_by_Allan._R._Hambley/chapter1_1.ipynb M 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Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter26_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter3_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter4_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter5_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter6_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter7_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/Chapter9_2.ipynb M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/README.txt M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/screenshots/image1.png M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/screenshots/image2.png M Numerical_Methods_For_Engineers_by_S._C._Chapra_And_R._P._Canale/screenshots/image3.png M Optical_Fiber_Communication_System_by_Dr._M.K._Raina/README.txt 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+{
+ "cells": [
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "# Chapter 18:Elements of Heat Transfer"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.1:pg-757"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 26,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.1\n",
+      "\n",
+      "\n",
+      " The rate of heat removal is  486.40484238  W\n",
+      "\n",
+      " Temperature at inside surface of brick is  20.2812224957  degree celcius\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "ho = 12.0 # Outside convective heat transfer coefficient in W/m**2K \n",
+    "x1 = 0.23# Thickness of brick in m\n",
+    "k1 = 0.98 # Thermal conductivity of brick in W/mK\n",
+    "x2 = 0.08 # Thickness of foam in m\n",
+    "k2 = 0.02# Thermal conductivity of foam in W/mK\n",
+    "x3 = 1.5# Thickness of wood in cm\n",
+    "k3 = 0.17# Thermal conductivity of wood in W/cmK\n",
+    "hi = 29.0# Inside convective heat transfer coefficient in W/m**2K \n",
+    "A = 90.0 # Total wall area in m**2\n",
+    "to = 22.0# outside air temperature in degree Celsius\n",
+    "ti = -2.0 # Inside air temperature in degree Celsius\n",
+    "print \"\\n Example 18.1\\n\"\n",
+    "U = (1/((1/ho)+(x1/k1)+(x2/k2)+(x3*1e-2/k3)+(1/hi)))# Overall heat transfer coefficient\n",
+    "Q = U*A*(to-ti) # Rate of heat transfer\n",
+    "R = (1/ho)+(x1/k1)\n",
+    "t2 = to-Q*R/A # Temperature at inside surface of brick\n",
+    "\n",
+    "print \"\\n The rate of heat removal is \",Q ,\" W\"\n",
+    "\n",
+    "print \"\\n Temperature at inside surface of brick is \",t2 ,\" degree celcius\"\n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.2:pg-758"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 8,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.2\n",
+      "\n",
+      "\n",
+      " Heat transfer rate is  2.33519645654  kW\n"
+     ]
+    }
+   ],
+   "source": [
+    "import math\n",
+    "r1 = 5.0 # Inner radius of steel pipe in cm\n",
+    "r2 = 10.0 # Extreme radius of inner insulation in cm\n",
+    "r3 = 13.0# Extreme radius of outer insulation in cm\n",
+    "K1 = 0.23 # Thermal conductivity of inner insulation in W/mK\n",
+    "K2 = 0.37 # Thermal conductivity of outer insulation in W/mK\n",
+    "hi = 58.0 # Inner heat transfer coefficient in W/m**2K\n",
+    "h0 = 12.0 # Inner heat transfer coefficient in W/m**2K\n",
+    "ti = 60.0 # Inner temperature in degree Celsius\n",
+    "to = 25.0 # Outer temperature in degree Celsius\n",
+    "L = 50.0 # Length of pipe in m\n",
+    "\n",
+    "print \"\\n Example 18.2\\n\"\n",
+    "Q =((2*math.pi*L*(ti-to))/((1/(hi*r1*1e-2))+(math.log(r2/r1)/(K1))+(math.log(r3/r2)/(K2))+(1/(h0*r3*1e-2))))\n",
+    "# Rate of heat transfer\n",
+    "print \"\\n Heat transfer rate is \",Q/1e3 ,\" kW\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.3:pg-759"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 9,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.3\n",
+      "\n",
+      "\n",
+      " Thermal conductivity of rod A is  57.4969670417  W/mK\n",
+      "\n",
+      " Thermal conductivity of rod B is  86.076212035  W/mK\n",
+      "\n",
+      " Thermal conductivity of rod C is  116.0  W/mK\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "to = 20 # Environment temperature in degree Celsius\n",
+    "t = 100# Temperature of steam path in degree Celsius\n",
+    "ta1 =  26.76 # Temperature at other end in degree Celsius for rod A \n",
+    "d = 10 # diameter of rod in mm\n",
+    "L = 0.25 # length of rod in m\n",
+    "h = 23 # heat transfer coefficient in W/m**2 K\n",
+    "tb1 =  32.00 # Temperature at other end in degree Celsius for rod B \n",
+    "tc1 =  36.93 # Temperature at other end in degree Celsius for rod C \n",
+    "\n",
+    "print \"\\n Example 18.3\\n\"\n",
+    "A = math.pi/4 * (d*1e-3)**2 #Area of rod\n",
+    "p = math.pi*d*1e-3 # perimeter of rod\n",
+    "# For rod A\n",
+    "a = (ta1-to)/(t-to) \n",
+    "ma = (math.acosh(1/a))/L\n",
+    "\n",
+    "Ka = (h*p)/(ma**2*A) # Thermal conductivity of rod A\n",
+    "print \"\\n Thermal conductivity of rod A is \",Ka ,\" W/mK\"\n",
+    "# For rod B\n",
+    "b = (tb1-to)/(t-to) \n",
+    "mb = (math.acosh(1/b))/L\n",
+    "\n",
+    "Kb = (h*p)/(mb**2*A) # Thermal conductivity of rod B\n",
+    "print \"\\n Thermal conductivity of rod B is \",Kb ,\" W/mK\"\n",
+    "c = (tc1-to)/(t-to) \n",
+    "mc = (math.acosh(1/c))/L\n",
+    "\n",
+    "Kc = (h*p)/(mc**2*A) # Thermal conductivity of rod A\n",
+    "print \"\\n Thermal conductivity of rod C is \",math. ceil(Kc) ,\" W/mK\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.4:pg-760"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 14,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.4\n",
+      "\n",
+      "\n",
+      " Midway temperature of rod is  88.7138777413  degree Celcius\n",
+      "\n",
+      " Heat loss rate is  88.0331604603 W\n"
+     ]
+    }
+   ],
+   "source": [
+    "h = 17.4 # Convective heat transfer coefficient in W/m**2K\n",
+    "K = 52.2 # Thermal conductivity in W/mK\n",
+    "t = 120 # Heat reservoir wall temperature in degree celcius\n",
+    "t0 = 35 # Ambient temperature in degree celcius\n",
+    "L = 0.4 # Lenght of rod in m\n",
+    "b  = .050 # width of rod in mm\n",
+    "H = .050 # Heigth of rod in mm\n",
+    "\n",
+    "print \"\\n Example 18.4\\n\"\n",
+    "l= L/2\n",
+    "A = b*H\n",
+    "m = math.sqrt(4*h*b/(K*b*H))\n",
+    "t1 = (t-t0)/math.cosh(m*l) + t0 # Midway temperature of rod\n",
+    "Q1 = 2*5.12*K*A*(t-t0)*math.tanh(m*l) # Heat loss rate \n",
+    "print \"\\n Midway temperature of rod is \",t1 ,\" degree Celcius\"\n",
+    "print \"\\n Heat loss rate is \",Q1 ,\"W\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.5:pg-760"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 16,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.5\n",
+      "\n",
+      "\n",
+      " Time to cool down to 2 degree celcius is  30.5933342864  min\n",
+      "\n",
+      " Temperature of peas after 10 minutes is  13.1714792663  degree celcius\n",
+      "\n",
+      " Temperature of peas after 30 minutes is  1.0393274697  degree celcius\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "d = 8.0 # Average diameter in mm\n",
+    "r = 750.0 # Density in Kg/m**3\n",
+    "t = 2.0 # Intermediate temperature in degree celcius\n",
+    "t_inf = 1.0 # Ambient temperature in degree celcius\n",
+    "t0 = 25.0 # Initial temperature in degree celcius\n",
+    "c = 3.35 # Specific heat in kJ/KgK\n",
+    "h = 5.8 # Heat transfer coeeficient in W/m**2K\n",
+    "T1 = 10.0 # time period in minutes\n",
+    "T2 = 30.0 # time period in minutes \n",
+    "t1 = 5.0 # Intermediate temperature in degree celcius\n",
+    "print \"\\n Example 18.5\\n\"\n",
+    "tau1 = c*1e3*math.log((t0-t_inf)/(t-t_inf))/(h*60) # Time to cool down to 2 degree celcius\n",
+    "tau2 = (t0-t_inf)*(math.exp(-(c*T1*60)/(c*1e3))) # Temperature of peas after 10 minutes\n",
+    "Y = math.exp(-1*(c*T2*60)/(c*1e3))\n",
+    "tau3 = (t0*Y-t1)/(Y-1)\n",
+    "\n",
+    "print \"\\n Time to cool down to 2 degree celcius is \",tau1 ,\" min\"\n",
+    "print \"\\n Temperature of peas after 10 minutes is \",tau2 ,\" degree celcius\"\n",
+    "print \"\\n Temperature of peas after 30 minutes is \",tau3 ,\" degree celcius\"\n",
+    "#The answers given in book are incorrect\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.6:pg-761"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 18,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.6\n",
+      "\n",
+      "\n",
+      " Surface area of heat exchanger is  53.1155468795  m**2\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "mh =  1000 # mass flow rate of hot fluid in Kg/h\n",
+    "mc = 1000 # mass flow rate of cold fluid in Kg/h\n",
+    "ch = 2.09 # Specific heat capacity of hot fluid in kJ/kgK\n",
+    "cc = 4.187 #Specific heat capacity of cold fluid in kJ/kgK \n",
+    "th1 = 80# Inlet temperature of hot fluid in degree celcius\n",
+    "th2 = 40 # Exit temperature of hot fluid in degree Celsius\n",
+    "tc1 = 30 # Inlet temperature of cold fluid in degree Celsius\n",
+    "U = 24 # heat transfer coefficient in W/m**2K\n",
+    "\n",
+    "print \"\\n Example 18.6\\n\"\n",
+    "Q = mh*ch*(th1-th2)\n",
+    "tc2 = Q/(mc*cc) + tc1# outlet temperature of cold fluid\n",
+    "te = th2-tc1 # Exit end temperature difference in degree Celsius\n",
+    "ti = th1 - tc2 # Inlet end temperature  difference in degree Celsius\n",
+    "t_lm = (ti-te)/(math.log(ti/te))\n",
+    "A = Q / (U*t_lm*3.6) # Surface are of heat exchanger\n",
+    "\n",
+    "print \"\\n Surface area of heat exchanger is \",A ,\" m**2\"\n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.7:pg-762"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 20,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.7\n",
+      "\n",
+      "\n",
+      " Surface area of heat exchanger is  3.52948841744  m**2\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "Hfg = 2257.0 # Latent heat at 100 degree Celsius\n",
+    "\n",
+    "ma =  500.0 # mass flow rate of air in Kg/h\n",
+    "ch = 1.005 # Specific heat capacity of hot air in kJ/kgK\n",
+    "ta1 = 260.0 # Inlet temperature of hot air in degree Celsius\n",
+    "ta2 = 150.0 # Inlet temperature of cold air in degree Celsius\n",
+    "tc1 = 100.0 # Inlet temperature of steam\n",
+    "tc2 = tc1 # Exit temperature of steam\n",
+    "U = 46.0 # heat transfer coefficient in W/m**2K\n",
+    "\n",
+    "print \"\\n Example 18.7\\n\"\n",
+    "Q = ma*ch*(ta1-ta2)\n",
+    "m = Q/Hfg # mass flow rate of steam\n",
+    "te = ta2-tc1 # Exit end temperature difference in degree Celsius\n",
+    "ti = ta1 - tc2 # Inlet end temperature  difference in degree Celsius\n",
+    "t_lm = (ti-te)/(math.log(ti/te))\n",
+    "A = Q / (U*t_lm*3.6) # Surface are of heat exchanger\n",
+    "\n",
+    "print \"\\n Surface area of heat exchanger is \",A ,\" m**2\"\n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.8:pg-763"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 21,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.8\n",
+      "\n",
+      "\n",
+      " Exit temperature of oil is  90.1251029717  degree celcius\n",
+      "\n",
+      " Rate of heat transfer is  1302.7384927  kW\n"
+     ]
+    }
+   ],
+   "source": [
+    "import math\n",
+    "mh =  20.15 # mass flow rate of hot fluid in Kg/s\n",
+    "mc = 5.04 # mass flow rate of cold fluid in Kg/h\n",
+    "ch = 2.094 # Specific heat capacity of hot fluid in kJ/kgK\n",
+    "cc = 4.2 #Specific heat capacity of cold fluid in kJ/kgK \n",
+    "th1 = 121# Inlet temperature of hot fluid in degree Celsius\n",
+    "th2 = 40 # Exit temperature of hot fluid in degree Celsius\n",
+    "tc1 = 10 # Inlet temperature of cold fluid in degree Celsius\n",
+    "U = 0.34 # heat transfer coefficient in kW/m**2K\n",
+    "n = 200 # total number of tubes\n",
+    "l = 4.87 # length of tube in m\n",
+    "d = 1.97 # Outer diameter in cm\n",
+    "print \"\\n Example 18.8\\n\"\n",
+    "A = math.pi*n*d*1e-2*l # Total surface area\n",
+    "mc_oil = mh*ch\n",
+    "mc_water = mc*cc\n",
+    "c_min = mc_water\n",
+    "c_max =mc_oil\n",
+    "    \n",
+    "if (mc_oil<mc_water):\n",
+    "    c_min = mc_oil\n",
+    "    c_max =mc_water\n",
+    "\n",
+    "R = c_min/c_max\n",
+    "NTU = U*A/c_min\n",
+    "e = (1-math.exp(-1*NTU*(1-R)))/(1-R*math.exp(-1*NTU*(1-R)))\n",
+    "t_larger = e*(th1-tc1)\n",
+    "t_water = t_larger \n",
+    "t_oil = t_water*mc_water/mc_oil\n",
+    "th2 = th1 - t_oil # Exit temperature of oil\n",
+    "Q = mh*ch*(th1-th2) # Rate of heat transfer\n",
+    "\n",
+    "print \"\\n Exit temperature of oil is \",th2 ,\" degree celcius\"\n",
+    "print \"\\n Rate of heat transfer is \",Q ,\" kW\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.9:pg-763"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 22,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.9\n",
+      "\n",
+      "\n",
+      " Heat transfer coefficient is  4074.68413756  W/m**2K\n",
+      "\n",
+      " Rate of heat transfer is  38.4029932568  kW\n"
+     ]
+    }
+   ],
+   "source": [
+    "u_m = 0.8 # mean velocity in m/s\n",
+    "D = 5 # Diameter in cm\n",
+    "v = 4.78e-7 # dynamic coefficient of viscosity\n",
+    "Pr = 2.98 # Prantl number\n",
+    "K = 0.66 # Thermal conductivity in W/mK\n",
+    "l = 3 # length of pipe in m\n",
+    "tw = 70 # Wall temperature\n",
+    "tf = 50 # mean water temperature\n",
+    "print \"\\n Example 18.9\\n\"\n",
+    "Re = u_m*D*1e-2/v # Reynold number\n",
+    "Nu = 0.023*(Re**0.8)*(Pr**0.4)\n",
+    "h = K*Nu/(D*1e-2) # Heat transfer coefficient\n",
+    "A = math.pi*D*1e-2*l # Surface area\n",
+    "Q = h*A*(tw-tf) # Rate of heat transfer\n",
+    "print \"\\n Heat transfer coefficient is \",h ,\" W/m**2K\"\n",
+    "print \"\\n Rate of heat transfer is \",Q/1e3 ,\" kW\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.10:pg-764"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 23,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.10\n",
+      "\n",
+      "\n",
+      " Rate of heat dissipation is  31.392  W\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "b = 10 # width of plate in cm\n",
+    "h = 15 # Height of plate in cm\n",
+    "hr = 8.72 # Radiative heat transfer coefficient in W/m**2K\n",
+    "tw = 140 # temperature of wall in degree Celsius\n",
+    "tf = 20 # Atmospheric temperature in degree Celsius\n",
+    "v = 2.109e-5 # Coefficient of dynamic viscosity in m**2/s\n",
+    "Pr = 0.692 # Prantl number\n",
+    "K = 0.0305 # Thermal conductivity in W/mK\n",
+    "L = 0.15 # characteristic length in m\n",
+    "g = 9.81 # Gravitational acceleration in m/s**2\n",
+    "\n",
+    "print \"\\n Example 18.10\\n\"\n",
+    "A = 2*b*1e-2*h*1e-2 # total area of plate\n",
+    "t_mean = (tw+tf)/2 +273\n",
+    "B = 1/t_mean\n",
+    "del_t = tw-tf\n",
+    "Gr = g*B*del_t*L**3/v**2 # Grashoff number\n",
+    "x = Gr*Pr\n",
+    "Nu = 0.59*(Gr*Pr)**0.25\n",
+    "hc = Nu*K/L\n",
+    "Q = (hc+hr)*A*del_t # Rate of heat dissipation\n",
+    "print \"\\n Rate of heat dissipation is \",Q ,\" W\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.11:pg-765"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 24,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.11\n",
+      "\n",
+      "\n",
+      " Time required for heating operation is  27.6219838873  s\n"
+     ]
+    }
+   ],
+   "source": [
+    "d1 = 2.0 # Diameter of steel rod in cm\n",
+    "d2 = 16.0 # Diameter of cylindrical furnace in cm\n",
+    "e1 = 0.6 # emissivity of inner surface\n",
+    "e2 = 0.85 # emissivity of rod surface\n",
+    "T = 1093.0 # Inner surface temperature of furncae in degree celcius\n",
+    "Tr1 = 427.0 # Initial temperature of rod in degree celcius\n",
+    "Tr2 = 538.0 # Initial temperature of rod in degree celcius\n",
+    "sigma = 5.67e-8 # Constant\n",
+    "rho = 7845.0 # density in kg/ m**3\n",
+    "c = 0.67 # Specific heat capacity in kJ/kgK\n",
+    "print \"\\n Example 18.11\\n\"\n",
+    "A_ratio = d1/d2 # Surface area ratio of cylindrical bodies\n",
+    "F12 = (1/((1/e1)+(A_ratio*(1/e2 -1))))\n",
+    "A1 = math.pi*d1*1e-2*1 # Surface area of rod\n",
+    "T1 = Tr1+273\n",
+    "T2 = T +273\n",
+    "T3 = Tr2 +273\n",
+    "Qi = sigma*A1*F12*(T1**4-T2**4)\n",
+    "Qe = sigma*A1*F12*(T3**4-T2**4)\n",
+    "\n",
+    "Q_avg = abs((Qi+Qe)/2)\n",
+    "tau = rho*c*(1e-4)*math.pi*(Tr2-Tr1)/(Q_avg*(1e-3))\n",
+    "\n",
+    "# Time required for heating operation \n",
+    "print \"\\n Time required for heating operation is \",tau ,\" s\"\n",
+    "\n",
+    "#The answers vary due to round off error\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex18.12:pg-765"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 25,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 18.12\n",
+      "\n",
+      "\n",
+      " Net heat transfer between two cylinders is  7297.2729358  W/m length\n",
+      "\n",
+      " Example 18.12\n",
+      "\n",
+      "\n",
+      " Net heat transfer between two cylinders is  7297.2729358  W/m length\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "d1 = 10.0 # Diameter of inner cylinder in cm\n",
+    "d2 = 20.0 # Diameter of outer cylinder in cm\n",
+    "e1 = 0.65 # emissivity of inner surface\n",
+    "e2 = 0.4 # emissivity of outer surface\n",
+    "T1 = 1000.0 # Inner surface temperature in K\n",
+    "T2 = 500.0 # outer suface temperature in K\n",
+    "sigma = 5.67e-8 # Constant\n",
+    "print \"\\n Example 18.12\\n\"\n",
+    "A1 = math.pi*d1*1e-2\n",
+    "A2 = math.pi*d2*1e-2\n",
+    "R =(((1-e1)/(e1*A1))+((1-e2)/(e2*A2))+(1/(A1*1)))\n",
+    "Eb1 = sigma*T1**4\n",
+    "Eb2 = sigma*T2**4\n",
+    "Q = (Eb1-Eb2)/R # Net heat transfer between two cylinders\n",
+    "print \"\\n Net heat transfer between two cylinders is \",Q ,\" W/m length\"\n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\n",
+    "d1 = 10.0 # Diameter of inner cylinder in cm\n",
+    "d2 = 20.0 # Diameter of outer cylinder in cm\n",
+    "e1 = 0.65 # emissivity of inner surface\n",
+    "e2 = 0.4 # emissivity of outer surface\n",
+    "T1 = 1000.0 # Inner surface temperature in K\n",
+    "T2 = 500.0 # outer surface temperature in K\n",
+    "sigma = 5.67e-8 # Constant\n",
+    "print \"\\n Example 18.12\\n\"\n",
+    "A1 = math.pi*d1*1e-2\n",
+    "A2 = math.pi*d2*1e-2\n",
+    "R =(((1-e1)/(e1*A1))+((1-e2)/(e2*A2))+(1/(A1*1)))\n",
+    "Eb1 = sigma*T1**4\n",
+    "Eb2 = sigma*T2**4\n",
+    "Q = (Eb1-Eb2)/R # Net heat transfer between two cylinders\n",
+    "print \"\\n Net heat transfer between two cylinders is \",Q ,\" W/m length\"\n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\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": "2.7.11"
+  }
+ },
+ "nbformat": 4,
+ "nbformat_minor": 0
+}
author	Trupti Kini	2016-09-02 23:32:06 +0600
committer	Trupti Kini	2016-09-02 23:32:06 +0600
commit	b417454ff6b5f8c2eb90f054723965a8f52e0268 (patch)
tree	466011c3926650f317396f0330586156abe58609 /Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter18.ipynb
parent	a001e64f70ee1aaf6051d6e25ca337ca680effb3 (diff)
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