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 10: Properties of gases and gas mixture"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.1:pg-366"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 9,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.1\n",
+      "\n",
+      "\n",
+      " The final equilibrium pressure is  1.16869318853  MPa\n",
+      "\n",
+      " The amount of heat transferred to the surrounding is  -226.04503125  kJ\n",
+      " \n",
+      "\n",
+      " If the vessel is perfectly insulated\n",
+      "\n",
+      " The final temperature is  45.4545454545  degree Celsius\n",
+      "\n",
+      " The final pressure is  1.24058552709  MPa\n"
+     ]
+    }
+   ],
+   "source": [
+    "Pa = 1.5 # Pressure in vessel A in MPa\n",
+    "Ta = 50  # Temperature in vessel A in K\n",
+    "ca = 0.5 # Content in vessel A in kg mol\n",
+    "Pb = 0.6 # Pressure in vessel B in MPa\n",
+    "Tb = 20 # Temperature in vessel B in K\n",
+    "mb = 2.5 # Content in vessel B in kg mol\n",
+    "R = 8.3143 # Universal gas constant\n",
+    "Va = (ca*R*(Ta+273))/(Pa*1e03) # volume of vessel A\n",
+    "ma = ca*28 # mass of gas in vessel A\n",
+    "Rn = R/28 # Gas content to of nitrogen\n",
+    "Vb = (mb*Rn*(Tb+273))/(Pb*1e03) # volume of vessel B\n",
+    "V = Va + Vb  # Total volume\n",
+    "m = ma + mb # Total mass\n",
+    "Tf = 27 # Equilibrium temperature in degree Celsius\n",
+    "P = (m*Rn*(Tf+273))/V # Equilibrium pressure \n",
+    "g = 1.4 # Heat capacity ratio\n",
+    "cv  = Rn/(g-1) # Heat capacity at constant volume\n",
+    "U1 = cv*(ma*Ta+mb*Tb) # Initial internal energy \n",
+    "U2 = m*cv*Tf# Final internal energy \n",
+    "Q = U2-U1 # heat transferred\n",
+    "\n",
+    "print \"\\n Example 10.1\"\n",
+    "print \"\\n\\n The final equilibrium pressure is \",P/1e3 ,\" MPa\"\n",
+    "print \"\\n The amount of heat transferred to the surrounding is \",Q ,\" kJ\"\n",
+    "#The answers vary due to round off error\n",
+    "\n",
+    "T_ = (ma*Ta+mb*Tb)/m  # final temperature\n",
+    "P_ = (m*Rn*(T_+273))/V # final pressure\n",
+    "print \" \\n\\n If the vessel is perfectly insulated\"\n",
+    "print \"\\n The final temperature is \",T_ ,\" degree Celsius\"\n",
+    "print \"\\n The final pressure is \",P_/1e3 ,\" MPa\""
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.2:pg-368"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 10,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.2\n",
+      "\n",
+      "\n",
+      " Gas constant of the gas is  0.461  kJ/kg K \n",
+      "\n",
+      " Molecular weight the gas is  18.0347071584  kg/kg mol\n",
+      "\n",
+      " The heat transfer at constant volume is  286.33  kJ\n",
+      "\n",
+      " Work done is  0  kJ\n",
+      "\n",
+      " The change in internal energy is  286.33  kJ\n",
+      "\n",
+      " The change in  enthalpy is  373.92  kJ\n",
+      "\n",
+      " The change in  entropy is  0.0  kJ/k\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "cp = 1.968 # Heat capacity in kJ/kg\n",
+    "cv = 1.507 # Heat capacity in kJ/kg\n",
+    "R_ = 8.314 # Gas constant\n",
+    "V = 0.3 # Volume of chamber in m**3\n",
+    "m = 2 # mass of gas in kg\n",
+    "T1 = 5# Initial gas temperature in degree Celsius\n",
+    "T2 = 100 # Final gas temperature in degree Celsius\n",
+    "R = cp-cv # Universal gas constant\n",
+    "mu = R_/R # molecular weight\n",
+    "Q12 = m*cv*(T2-T1) # The heat transfer at constant volume\n",
+    "W12 = 0 # work done\n",
+    "U21 = Q12 # change in internal energy\n",
+    "H21= m*cp*(T2-T1) # change in  enthalpy\n",
+    "S21 = m*cv*math.log((T2+273)/(T1+273)) #change in  entropy \n",
+    "\n",
+    "print \"\\n Example 10.2\"\n",
+    "print \"\\n\\n Gas constant of the gas is \",R ,\" kJ/kg K \"\n",
+    "print \"\\n Molecular weight the gas is \",mu ,\" kg/kg mol\"\n",
+    "print \"\\n The heat transfer at constant volume is \",Q12 ,\" kJ\"\n",
+    "print \"\\n Work done is \",0 ,\" kJ\"\n",
+    "print \"\\n The change in internal energy is \",U21 ,\" kJ\"\n",
+    "print \"\\n The change in  enthalpy is \",H21 ,\" kJ\"\n",
+    "print \"\\n The change in  entropy is \",S21 ,\" kJ/k\"\n",
+    "#The answers vary due to round off error\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.3:pg-369"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 11,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.3\n",
+      "\n",
+      " The work done in the expansion is  300.72200185  kJ\n"
+     ]
+    }
+   ],
+   "source": [
+    "import math\n",
+    "from scipy import integrate\n",
+    "m = 1.5 # Mass of gas in kg\n",
+    "P1 = 5.6 # Initial pressure of gas in MPa\n",
+    "V1 = 0.06 # Initial volume of gas in m**3\n",
+    "T2_ = 240 # Final temperature of gas in degree Celsius\n",
+    "a = 0.946 # Constant\n",
+    "b = 0.662 # Constant\n",
+    "k = 1e-4 # Constant\n",
+    "# Part (b)\n",
+    "R = a-b # constant\n",
+    "T2 = T2_+273 # Final temperature of gas in KK\n",
+    "T1 = (P1*1e03*V1)/(m*R) # Initial temperature\n",
+    "W12,er =integrate.quad(lambda T:m*(b+k*T),T1,T2) # Work done\n",
+    "\n",
+    "print \"\\n Example 10.3\"\n",
+    "print \"\\n The work done in the expansion is \",-W12 ,\" kJ\"\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.5:pg-371"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 12,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.5\n",
+      "\n",
+      " The work transfer for the whole path is  93.4986082985  kJ\n",
+      "\n",
+      " The heat transfer for the whole path  571.638005316  kJ\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "m = 0.5 # mass of air in kg\n",
+    "P1 = 80 # Initial pressure kPa\n",
+    "T1 = 60 # Initial temperature in degree Celsius\n",
+    "P2 = 0.4 # Final pressure in MPa\n",
+    "R = 0.287 # Gas constant\n",
+    "V1 = (m*R*(T1+273))/(P1) # Volume of air at state 1\n",
+    "g = 1.4 # Heat capacity ratio\n",
+    "T2 = (T1+273)*(P2*1e3/P1)**((g-1)/g)# Final temperature\n",
+    "W12 = (m*R*(T1+273-T2))/(g-1) # Work done in \n",
+    "V2 = V1*((P1/(P2*1e3))**(1/g)) # Final volume\n",
+    "W23 = P2*(V1-V2)*1e3 # # Work done\n",
+    "W = W12+W23 # Net work done\n",
+    "V3 = V1 # constant volume\n",
+    "T3 = (T2)*(V3/V2) # Temperature at state 3\n",
+    "cp = 1.005 # Heat capacity at constant volume in kJ/kgK\n",
+    "Q = m*cp*(T3-T2)# Heat transfer\n",
+    "print \"\\n Example 10.5\"\n",
+    "print \"\\n The work transfer for the whole path is \",W ,\" kJ\"\n",
+    "#The answers vary due to round off error\n",
+    "print \"\\n The heat transfer for the whole path \",Q ,\" kJ\"\n",
+    "#The answer provided in the textbook is wrong\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.6:pg-372"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 13,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.6\n",
+      "\n",
+      " The heat received in the cycle is  137.268292683  kJ\n",
+      "\n",
+      " The heat rejected in the cycle  84.2666952566  kJ\n",
+      "\n",
+      " The efficiency of the cycle is  39.0  percent\n"
+     ]
+    }
+   ],
+   "source": [
+    "P1 = 700 # Initial pressure of gas in kPa\n",
+    "T1 = 260 # Initial temperature of gas in degree Celcius \n",
+    "T3 = T1 # Temperature at state 3\n",
+    "V1 = 0.028 # Initial volume of gas in m**3\n",
+    "V2 = 0.084 # Final volume of gas in m**3\n",
+    "R = 0.287 # Gas constant\n",
+    "m = (P1*V1)/(R*(T1+273)) # mass of gas  \n",
+    "P2 = P1 # Pressure at state 2\n",
+    "T2 = (T1+273)*((P2*V2)/(P1*V1)) # Temperature at state 2\n",
+    "n  = 1.5 # polytropic index \n",
+    "P3 = P2*(((T3+273)/(T2))**(n/(n-1))) # Pressure at state 3\n",
+    "cp = 1.005 # COnstant pressure heat capacity in kJ/kgK\n",
+    "cv = 0.718 # COnstant volume heat capacity in kJ/kgK\n",
+    "Q12 = m*cp*(T2-T1-273) # HEat transfer\n",
+    "Q23 = m*cv*(T3+273-T2) + (m*R*(T2-T3-273))/(n-1) # Heat transfer\n",
+    "Q31 = m*R*(T1+273)*math.log(P3/P2) # Heat transfer\n",
+    "Q1 = Q12 # Heat equivalance\n",
+    "Q2 = -(Q23+Q31) # Net heat transfer\n",
+    "e = 1-(Q2/Q1) # First law efficiency\n",
+    "\n",
+    "print \"\\n Example 10.6\"\n",
+    "print \"\\n The heat received in the cycle is \",Q1 ,\" kJ\"\n",
+    "print \"\\n The heat rejected in the cycle \",Q2 ,\" kJ\"\n",
+    "print \"\\n The efficiency of the cycle is \",math. ceil(e*100) ,\" percent\"\n",
+    "#The answers vary due to round off error"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.7:pg-374"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 14,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.7\n",
+      "\n",
+      " Cv of the gas is  0.661000944287  kJ/kg K\n",
+      "\n",
+      " Cp of the gas is  0.89896128423  kJ/kg K\n",
+      "\n",
+      " Increase in the entropy of the gas is  0.080159241414  kJ/kg K\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "P1 = 300 # Initial gas pressure in kPa\n",
+    "V1 = 0.07 # Initial volume of gas in m**3\n",
+    "m = 0.25 # Mass of gas in kg\n",
+    "T1 = 80 # Initial temperature of gas in degree Celsius\n",
+    "R = (P1*V1)/(m*(T1+273)) # constant\n",
+    "P2 = P1 # process condition\n",
+    "V2 = 0.1 # Final volume in m**3\n",
+    "T2 = (P2*V2)/(m*R) # Final temperature in K\n",
+    "W = -25 #Work done in kJ\n",
+    "cv = -W/(m*(T2-T1-273)) # Constant volume heat capacity in kJ/kg\n",
+    "cp = R+cv #Constant pressure heat capacity in kJ/kg\n",
+    "S21 = m*cp*math.log(V2/V1) # Entropy change\n",
+    "print \"\\n Example 10.7\"\n",
+    "print \"\\n Cv of the gas is \",cv ,\" kJ/kg K\"\n",
+    "print \"\\n Cp of the gas is \",cp ,\" kJ/kg K\"\n",
+    "print \"\\n Increase in the entropy of the gas is \",S21 ,\" kJ/kg K\"\n",
+    "#The answers vary due to round off error\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.8:pg-374"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 15,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.8\n",
+      "\n",
+      "\n",
+      " Mole fraction of N2 is  0.485294117647\n",
+      "\n",
+      " Mole fraction of CO2  is  0.514705882353\n",
+      "\n",
+      " Equivalent molecular weight of mixture is  36.2352941176 kg/kg mol\n",
+      "\n",
+      "\n",
+      " The equivalent gas constant of the mixture is  0.229444805195  kJ/kg K\n",
+      "\n",
+      "\n",
+      " Partial pressures of nitrogen and CO2 are \n",
+      "  145.588235294  kPa and  154.411764706  kPa respectively\n",
+      "\n",
+      " Partial volume of nitrogen and CO2 are \n",
+      "  0.870000714286  kPa and  0.922728030303  kPa respectively\n",
+      "\n",
+      "\n",
+      " Total volume of mixture is  1.79272874459  m**3\n",
+      "\n",
+      " Density of mixture is  4.46247098126  kg/m**3\n",
+      "\n",
+      "\n",
+      " Cp and Cv of mixture are \n",
+      "  0.920740483948 kJ/kg K and  0.691295678753 kJ/kg K respectively\n",
+      "\n",
+      "\n",
+      " Change in internal energy of the system heated at constant volume  is  110.6073086 kJ\n",
+      "\n",
+      " Change in enthalpy of the system heated at constant volume  is  147.318477432 kJ\n",
+      "\n",
+      " Change in entropy of the system heated at constant volume  is  0.36517324538  kJ/kg K\n",
+      "\n",
+      "\n",
+      " Change in entropy of the system heated at constant Pressure  is  0.486376236695 kJ/kgK\n"
+     ]
+    }
+   ],
+   "source": [
+    "import math\n",
+    "mn = 3.0 # Mass of nitrogen in kg\n",
+    "mc = 5.0 # mass of CO2 in kg\n",
+    "an = 28.0 # Atomic weight of nitrogen\n",
+    "ac = 44.0 # Atomic weight of CO2\n",
+    "# Part (a)\n",
+    "xn = (mn/an)/((mn/an)+(mc/ac)) # mole fraction of nitrogen\n",
+    "xc = (mc/ac)/((mn/an)+(mc/ac)) # mole fraction of carbon\n",
+    "\n",
+    "print \"\\n Example 10.8\"\n",
+    "print \"\\n\\n Mole fraction of N2 is \",xn \n",
+    "print \"\\n Mole fraction of CO2  is \",xc\n",
+    "#The answers vary due to round off error\n",
+    "\n",
+    "# Part (b)\n",
+    "M = xn*an+xc*ac # Equivalent molecular weight\n",
+    "print \"\\n Equivalent molecular weight of mixture is \",M ,\"kg/kg mol\" \n",
+    "\n",
+    "# Part (c)\n",
+    "R = 8.314 # Gas constant\n",
+    "Req = ((mn*R/an)+(mc*R/ac))/(mn+mc)\n",
+    "print \"\\n\\n The equivalent gas constant of the mixture is \",Req ,\" kJ/kg K\" \n",
+    "\n",
+    "# Part (d)\n",
+    "P = 300.0 # Initial pressure in kPa\n",
+    "T = 20.0 # Initial temperature in degree Celsius\n",
+    "Pn = xn*P # Partial pressure of Nitrogen\n",
+    "Pc = xc*P # Partial pressure of CO2 \n",
+    "Vn = (mn*R*(T+273))/(P*an) # Volume of nitrogen\n",
+    "Vc = (mc*R*(T+273))/(P*ac) # Volume of CO2\n",
+    "print \"\\n\\n Partial pressures of nitrogen and CO2 are \\n \",Pn ,\" kPa and \",Pc ,\" kPa respectively\"\n",
+    "print \"\\n Partial volume of nitrogen and CO2 are \\n \",Vn ,\" kPa and \",Vc ,\" kPa respectively\"\n",
+    "# Part (e)\n",
+    "V = (mn+mc)*Req*(T+273)/P # Total volume\n",
+    "rho = (mn+mc)/V # mass density\n",
+    "print \"\\n\\n Total volume of mixture is \",V ,\" m**3\" \n",
+    "print \"\\n Density of mixture is \",rho ,\" kg/m**3\" \n",
+    "\n",
+    "# Part (f)\n",
+    "gn = 1.4 # Heat capacity ratio for nitrogen\n",
+    "gc = 1.286 # Heat capacity ratio for carbon dioxide \n",
+    "cvn = R/((gn-1)*an) # cp and cv of N2\n",
+    "cpn = gn*cvn  # Constant pressure heat capacity of nitrogen\n",
+    "cvc = R/((gc-1)*ac) # cp and cv of CO2\n",
+    "cpc = gc*cvc# COnstant pressure heat capacity of carbon dioxide \n",
+    "cp = (mn*cpn+mc*cpc)/(mn+mc)  # Constant pressure heat capacity ratio of mixture\n",
+    "cv = (mn*cvn+mc*cvc)/(mn+mc) # Constant volume Heat capacity ratio of mixture\n",
+    "print \"\\n\\n Cp and Cv of mixture are \\n \",cp ,\"kJ/kg K and \",cv ,\"kJ/kg K respectively\" \n",
+    "T1 = T \n",
+    "T2 = 40 \n",
+    "U21 = (mn+mc)*cv*(T2-T1)\n",
+    "H21 = (mn+mc)*cp*(T2-T1)\n",
+    "S21v = (mn+mc)*cv*math.log((T2+273)/(T1+273)) # If heated at constant volume\n",
+    "S21p = (mn+mc)*cp*math.log((T2+273)/(T1+273)) # If heated at constant Pressure\n",
+    "\n",
+    "print \"\\n\\n Change in internal energy of the system heated at constant volume  is \",U21 ,\"kJ\" \n",
+    "print \"\\n Change in enthalpy of the system heated at constant volume  is \",H21 ,\"kJ\" \n",
+    "print \"\\n Change in entropy of the system heated at constant volume  is \",S21v ,\" kJ/kg K\"\n",
+    "print \"\\n\\n Change in entropy of the system heated at constant Pressure  is \",S21p ,\"kJ/kgK\" \n",
+    "\n",
+    "#The answers vary due to round off error\n",
+    "\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.9:pg-375"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 16,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.9\n",
+      "\n",
+      " Increase in entropy is  1.22920562691  kJ/kg K\n"
+     ]
+    }
+   ],
+   "source": [
+    "import math\n",
+    "mo = 2.0 # mass of oxygen in kg\n",
+    "mn = 6.0 # mass of nitrogen in kg\n",
+    "muo = 32.0 # molecular mass of oxygen\n",
+    "mun = 28.0 # molecular mass of nitrogen\n",
+    "o = mo/muo # mass fraction of oxygen\n",
+    "n = mn/mun # mass fraction of nitrogen\n",
+    "xo = o/(n+o) # mole fraction of oxygen\n",
+    "xn = n/(n+o) # mole fraction of nitrogen\n",
+    "R = 8.314 # Universal gas constant\n",
+    "Ro = R/muo # Gas constant for oxygen\n",
+    "Rn = R/mun # Gas constant for nitrogen\n",
+    "dS = -mo*Ro*math.log(xo)-mn*Rn*math.log(xn) # Increase in entropy \n",
+    "\n",
+    "print \"\\n Example 10.9\"\n",
+    "print \"\\n Increase in entropy is \",dS ,\" kJ/kg K\"\n",
+    "#The answers vary due to round off error\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Ex10.10:pg-376"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 10,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "\n",
+      " Example 10.10\n",
+      "\n",
+      " Specific volume is  3.05515367719  *10**-3 m3/kg\n",
+      "\n",
+      " Specific temperature is  57.85  K\n",
+      "\n",
+      " Specific pressure is  5.46  MPa\n",
+      "\n",
+      " Reduced volume is  1.48226362179  m3/kg\n"
+     ]
+    }
+   ],
+   "source": [
+    "\n",
+    "an = 20.183 # molecular weight of neon\n",
+    "Pc = 2.73 # Critical pressure\n",
+    "Tc = 44.5 # Critical tmperature in Kelvin\n",
+    "Vc = 0.0416 # volume of gas in m**3\n",
+    "Pr = 2 # Reduced Pressure\n",
+    "Tr = 1.3 # Reduced temperature\n",
+    "Z = 0.7 # Compressibility factor\n",
+    "P = Pr*Pc # Corresponding Pressure \n",
+    "T = Tr*Tc # Corresponding temperature\n",
+    "R = 8.314 # Gas constant\n",
+    "v = (Z*R*T)/(P*an) # Corresponding volume\n",
+    "vr = (v*an)/(Vc*1e3)  # reduced volume\n",
+    "\n",
+    "print \"\\n Example 10.10\"\n",
+    "print \"\\n Specific volume is \",v ,\" *10**-3 m3/kg\"\n",
+    "print \"\\n Specific temperature is \",T ,\" K\"\n",
+    "print \"\\n Specific pressure is \",P ,\" MPa\"\n",
+    "print \"\\n Reduced volume is \",vr ,\" m3/kg\"\n",
+    "#The answers vary due to round off error\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	3c5945f0aaf1d2d1f84e43ead6676aa497c9c4f8 (patch)
tree	875e29964798bb3c96b465cb07013dd68a30e106 /Basic_And_Applied_Thermodynamics_by_P._K._Nag/Chapter10.ipynb
parent	d4fdaaa0564be527ad6a83b727ea7ab4310ac840 (diff)
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