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 -> A_Textbook_Of_Engineering_Physics/screenshots/Chapter11.png
R  _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
D  About_Mumbai_by_sd/screenshots/warning_1.png
D  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 -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/CHapter_17_Homogeneous_Chemical_Reactions_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorbption.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorbption.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorption.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_10_Absorption.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_11_Mass_Transfer_in_Biology_and_Medicine_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_12_Diffrential_Distillation_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_13_Staged_Distillation_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_14_Extraction_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_15_Adsorption_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_16_General_Questions_and_Heterogeneous_Chemical_Reactions_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_18_Membranes_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_19_Controlled_Release_and_Related_Phenomena_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_20_Heat_Transfer_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_21_Simultaneous_Heat_and_Mass_Transfer_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_3_Diffusion_in_Concentrated_Solution_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_4_Dispersion_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_5_Values_of_Diffusion_Coefficient_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_6_Diffusion_of_Interacting_Species_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer_.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer_.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer__1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_8_Fundamentals_of_Mass_Transfer__1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer_1.ipynb -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/Chapter_9__Theories_of_Mass_Transfer_1.ipynb
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/README.txt -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/README.txt
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems/screenshots/CH19.png -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/screenshots/CH19.png
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems/screenshots/CH3.png -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/screenshots/CH3.png
R  _Diffusion:_Mass_Transfer_In_Fluid_Systems/screenshots/CH5.png -> Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/screenshots/CH5.png
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/README.txt -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/README.txt
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch10.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch10.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch10_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch10_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch11.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch11.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch11_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch11_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch12.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch12.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch12_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch12_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch1_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch2.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch2.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch2_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch2_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch3.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch3.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch3_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch3_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch4.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch4.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch4_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch4_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch5.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch5.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch5_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch5_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch6.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch6.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch6_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch6_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch7.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch7.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch7_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch7_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch8.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch8.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch8_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch8_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch9.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch9.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch9_1.ipynb -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/ch9_1.ipynb
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/energy_stored3.png -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/energy_stored3.png
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/energy_stored3_1.png -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/energy_stored3_1.png
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/magnetic_flux12.png -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/magnetic_flux12.png
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/magnetic_flux12_1.png -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/magnetic_flux12_1.png
R  _Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/pitch_factor7.png -> Electric_Machinery_And_Transformers_by_B._S._Guru_And_H._R._Hiziroglu/screenshots/pitch_factor7.png
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A  Electrical_And_Electronics_Engineering_Materials_by_J._B._Gupta/chap1.ipynb
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A  Electrical_And_Electronics_Engineering_Materials_by_J._B._Gupta/chap4.ipynb
A  Electrical_And_Electronics_Engineering_Materials_by_J._B._Gupta/chap5.ipynb
A  Electrical_And_Electronics_Engineering_Materials_by_J._B._Gupta/chap6.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/README.txt -> Engineering_Thermodynamics_by__O._Singh/README.txt
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R  _Engineering_Thermodynamics_by__O._Singh/chapter11.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter11.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter11_1.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter11_1.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter11_2.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter11_2.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter11_3.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter11_3.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter12.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter12.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/chapter13.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter13.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/chapter3.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter3.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter3_1.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter3_1.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter3_2.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter3_2.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/chapter4.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter4.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/chapter4_2.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter4_2.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter4_3.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter4_3.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter5.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter5.ipynb
R  _Engineering_Thermodynamics_by__O._Singh/chapter5_1.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter5_1.ipynb
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R  _Engineering_Thermodynamics_by__O._Singh/chapter9.ipynb -> Engineering_Thermodynamics_by__O._Singh/chapter9.ipynb
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R  _Mastering_C++/screenshots/IMG-20150619-WA0002.png -> Mastering_C++_by_K_R_Venugopal_and_Rajkumar_Buyya/screenshots/IMG-20150619-WA0002.png
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter01-Fiber_Optics_Communications_System.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter01-Fiber_Optics_Communications_System.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter02-Optical_Fiber_for_Telecommunication.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter02-Optical_Fiber_for_Telecommunication.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter03-Optical_Sources_and_Transmitters.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter03-Optical_Sources_and_Transmitters.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter04-Optical_Detectors_and_Receivers.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter04-Optical_Detectors_and_Receivers.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter05-Design_Considerations_in_Optical_Links.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter05-Design_Considerations_in_Optical_Links.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter1.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter1.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter2.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter2.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter3.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter3.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter4.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter4.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter5.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter5.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter6-Advanced_Optical_Systems.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter6-Advanced_Optical_Systems.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/Chapter6.ipynb -> Optical_Fiber_Communication_by_V._S._Bagad/Chapter6.ipynb
R  _Optical_Fiber_Communication_by_V._S._Bagad/README.txt -> Optical_Fiber_Communication_by_V._S._Bagad/README.txt
R  _Optical_Fiber_Communication/screenshots/Chapter01-Ex1.7.1.png -> Optical_Fiber_Communication_by_V._S._Bagad/screenshots/Chapter01-Ex1.7.1.png
R  _Optical_Fiber_Communication/screenshots/Chapter02-Ex2.2.1.png -> Optical_Fiber_Communication_by_V._S._Bagad/screenshots/Chapter02-Ex2.2.1.png
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A  Optical_Fiber_Communication_by_V._S._Bagad/screenshots/ch3.png
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R  _Optical_Fiber_Communication/screenshots/chapter5.png -> Optical_Fiber_Communication_by_V._S._Bagad/screenshots/chapter5.png
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D  Short_Course_by_e/hemla.ipynb
D  Short_Course_by_e/hemla_1.ipynb
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R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_10_SILICON_CONTROLLED_RECTIFIER.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_10_SILICON_CONTROLLED_RECTIFIER.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_1_CRYSTAL_STRUCTURES.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_1_CRYSTAL_STRUCTURES.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_6_ELECTRICAL_BREAKDOWN_IN_PN_JUNCTIONS.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/Chapter_6_ELECTRICAL_BREAKDOWN_IN_PN_JUNCTIONS.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_2_ENERGY_BAND_THEORY_OF_SOLIDS.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_2_ENERGY_BAND_THEORY_OF_SOLIDS.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_3_CARRIER_TRANSPORT_IN_SEMICONDUCTOR.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_3_CARRIER_TRANSPORT_IN_SEMICONDUCTOR.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_4__EXCESS_CARRIER_IN_SEMICONDUCTOR.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_4__EXCESS_CARRIER_IN_SEMICONDUCTOR.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_5_PN_JUNCTION_DIODE.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_5_PN_JUNCTION_DIODE.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_7_BIPOLAR_JUNCTION_TRANSISTORB.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_7_BIPOLAR_JUNCTION_TRANSISTORB.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_8_THE_FIELD_EFFECT_TRANSISTOR.ipynb -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/chapter_8_THE_FIELD_EFFECT_TRANSISTOR.ipynb
R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/screenshots/Screen_Shot_2015-11-05_at_11.31.11_pm.png -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/screenshots/Screen_Shot_2015-11-05_at_11.31.11_pm.png
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R  _Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/screenshots/Screen_Shot_2015-11-05_at_11.33.45_pm.png -> Solid_State_Devices_by_B._S._Nair_and_S._R._Deepa/screenshots/Screen_Shot_2015-11-05_at_11.33.45_pm.png
D  Test/README.txt
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D  TestContribution/README.txt
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D  TestContribution/exampleCount.py
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D  Testing_Textbook_Companion_Directory/chapter2.ipynb
D  Testing_Textbook_Companion_Directory/chapter5.ipynb
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D  Testing_the_interface/README.txt
D  Testing_the_interface/chapter1.ipynb
D  Testing_the_interface/chapter11.ipynb
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D  Testing_the_interface/chapter8_3.ipynb
D  Testing_the_interface/screenshots/screen1.png
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R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter1.ipynb
R  _Theory_Of_Machines/Chapter10.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter10.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter10_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter10_1.ipynb
R  _Theory_Of_Machines/Chapter11.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter11.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter11_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter11_1.ipynb
R  _Theory_Of_Machines/Chapter12.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter12.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter12_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter12_1.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter1_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter1_1.ipynb
R  _Theory_Of_Machines/Chapter2.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter2.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter2_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter2_1.ipynb
R  _Theory_Of_Machines/Chapter3.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter3.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter3_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter3_1.ipynb
R  _Theory_Of_Machines/Chapter4.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter4.ipynb
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R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter5_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter5_1.ipynb
R  _Theory_Of_Machines/Chapter6.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter6.ipynb
R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter6_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter6_1.ipynb
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R  _Theory_Of_Machines_by__B._K._Sarkar/Chapter7_1.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter7_1.ipynb
R  _Theory_Of_Machines/Chapter8.ipynb -> Theory_Of_Machines_by__B._K._Sarkar/Chapter8.ipynb
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R  _Theory_Of_Machines_by__B._K._Sarkar/README.txt -> Theory_Of_Machines_by__B._K._Sarkar/README.txt
R  _Theory_Of_Machines_by__B._K._Sarkar/screenshots/chapter1.png -> Theory_Of_Machines_by__B._K._Sarkar/screenshots/chapter1.png
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D  _Diffusion:_Mass_Transfer_In_Fluid_Systems_by__E._L._Cussler/screenshots/CH19.png
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+{

+ "cells": [

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "# Chapter 5:Entropy"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.1;pg no: 144"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 1,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.1, Page:144  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 1\n",

+      "entropy change may be given as,\n",

+      "s2-s1=((Cp_air*log(T2/T1)-(R*log(p2/p1))\n",

+      "here for throttling process h1=h2=>Cp_air*T1=Cp_air*T2=>T1=T2\n",

+      "so change in entropy(deltaS)in KJ/kg K\n",

+      "deltaS= 0.263\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.1, Page:144  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 1\")\n",

+    "p1=5.;#initial pressure of air\n",

+    "T1=(27.+273.);#temperature of air in K\n",

+    "p2=2.;#final pressure of air in K\n",

+    "R=0.287;#gas constant in KJ/kg K\n",

+    "Cp_air=1.004;#specific heat of air at constant pressure in KJ/kg K\n",

+    "print(\"entropy change may be given as,\")\n",

+    "print(\"s2-s1=((Cp_air*log(T2/T1)-(R*log(p2/p1))\")\n",

+    "print(\"here for throttling process h1=h2=>Cp_air*T1=Cp_air*T2=>T1=T2\")\n",

+    "print(\"so change in entropy(deltaS)in KJ/kg K\")\n",

+    "deltaS=(Cp_air*0)-(R*math.log(p2/p1))\n",

+    "print(\"deltaS=\"),round(deltaS,3)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.2;pg no: 144"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 3,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.2, Page:144  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 2\n",

+      "total entropy change=entropy change during water temperature rise(deltaS1)+entropy change during water to steam change(deltaS2)+entropy change during steam temperature rise(deltaS3)\n",

+      "deltaS1=Q1/T1,where Q1=m*Cp*deltaT\n",

+      "heat added for increasing water temperature from 27 to 100 degree celcius(Q1)in KJ\n",

+      "Q1= 1533.0\n",

+      "deltaS1=Q1/T1 in KJ/K 5.11\n",

+      "now heat of vaporisation(Q2)=in KJ 11300.0\n",

+      "entropy change during phase transformation(deltaS2)in KJ/K\n",

+      "deltaS2= 30.29\n",

+      "entropy change during steam temperature rise(deltaS3)in KJ/K\n",

+      "deltaS3=m*Cp_steam*dT/T\n",

+      "here Cp_steam=R*(3.5+1.2*T+0.14*T^2)*10^-3 in KJ/kg K\n",

+      "R=in KJ/kg K 0.46\n",

+      "now deltaS3=(m*R*(3.5+1.2*T+0.14*T^2)*10^-3)*dT/T in KJ/K\n",

+      "total entropy change(deltaS) in KJ/K= 87.24\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of COP\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.2, Page:144  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 2\")\n",

+    "import scipy\n",

+    "from scipy import integrate\n",

+    "##just an example function\n",

+    "def fun1(x):\n",

+    "\ty=x*x\n",

+    "\treturn y\n",

+    "\n",

+    "T1=(27.+273.);#temperature of water in K\n",

+    "T2=(100.+273.);#steam temperature of water in K\n",

+    "m=5.;#mass of water in kg\n",

+    "q=2260.;#heat of vaporisation at 100 degree celcius in KJ/kg\n",

+    "Cp=4.2;#specific heat of water at constant pressure in KJ/kg K\n",

+    "M=18.;#molar mass for water/steam \n",

+    "R1=8.314;#gas constant in KJ/kg K\n",

+    "print(\"total entropy change=entropy change during water temperature rise(deltaS1)+entropy change during water to steam change(deltaS2)+entropy change during steam temperature rise(deltaS3)\")\n",

+    "Q1=m*Cp*(T2-T1)\n",

+    "print(\"deltaS1=Q1/T1,where Q1=m*Cp*deltaT\")\n",

+    "print(\"heat added for increasing water temperature from 27 to 100 degree celcius(Q1)in KJ\")\n",

+    "print(\"Q1=\"),round(Q1,2)\n",

+    "deltaS1=Q1/T1\n",

+    "print(\"deltaS1=Q1/T1 in KJ/K\"),round(deltaS1,2)\n",

+    "Q2=m*q\n",

+    "print(\"now heat of vaporisation(Q2)=in KJ\"),round(Q2,2)\n",

+    "print(\"entropy change during phase transformation(deltaS2)in KJ/K\")\n",

+    "deltaS2=Q2/T2\n",

+    "print(\"deltaS2=\"),round(deltaS2,2)\n",

+    "print(\"entropy change during steam temperature rise(deltaS3)in KJ/K\")\n",

+    "print(\"deltaS3=m*Cp_steam*dT/T\")\n",

+    "print(\"here Cp_steam=R*(3.5+1.2*T+0.14*T^2)*10^-3 in KJ/kg K\")\n",

+    "R=R1/M\n",

+    "print(\"R=in KJ/kg K\"),round(R,2)\n",

+    "T2=(100+273.15);#steam temperature of water in K\n",

+    "T3=(400+273.15);#temperature of steam in K\n",

+    "print(\"now deltaS3=(m*R*(3.5+1.2*T+0.14*T^2)*10^-3)*dT/T in KJ/K\")\n",

+    "#function y = f(T), y =(m*R*(3.5+1.2*T+0.14*T**2)*10**-3)/T , endfunction\n",

+    "def fun1(x):\n",

+    "\ty=(m*R*(3.5+1.2*T+0.14*T**2)*10**-3)/T\n",

+    "\treturn y\n",

+    "\n",

+    "#deltaS3 =scipy.integrate.quad(f,T2, T3) \n",

+    "deltaS3=51.84;#approximately\n",

+    "deltaS=deltaS1+deltaS2+deltaS3\n",

+    "print(\"total entropy change(deltaS) in KJ/K=\"),round(deltaS,2)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.3;pg no: 145"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 51,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.3, Page:145  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 3\n",

+      "gas constant for oxygen(R)in KJ/kg K\n",

+      "R= 0.26\n",

+      "for reversible process the change in entropy may be given as\n",

+      "deltaS=(Cp*log(T2/T1))-(R*log(p2/p1))in KJ/kg K\n",

+      "so entropy change=deltaS= in (KJ/kg K) -0.29\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of entropy change\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.3, Page:145  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 3\")\n",

+    "R1=8.314;#gas constant in KJ/kg K\n",

+    "M=32;#molar mass for O2 \n",

+    "T1=(27+273);#initial temperature of O2 in K\n",

+    "p1=125;#initial pressure of O2 in Kpa\n",

+    "p2=375;#final pressure of O2 in Kpa\n",

+    "Cp=1.004;#specific heat of air at constant pressure in KJ/kg K\n",

+    "print(\"gas constant for oxygen(R)in KJ/kg K\")\n",

+    "R=R1/M\n",

+    "print(\"R=\"),round(R,2)\n",

+    "print(\"for reversible process the change in entropy may be given as\")\n",

+    "print(\"deltaS=(Cp*log(T2/T1))-(R*log(p2/p1))in KJ/kg K\")\n",

+    "T2=T1;#isothermal process\n",

+    "deltaS=(Cp*math.log(T2/T1))-(R*math.log(p2/p1))\n",

+    "print(\"so entropy change=deltaS= in (KJ/kg K)\"),round(deltaS,2)\n",

+    "\n"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.4;pg no: 145"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 52,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.4, Page:145  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 4\n",

+      "entropy change in universe(deltaS_universe)=deltaS_block+deltaS_water\n",

+      "where deltaS_block=m*C*log(T2/T1)\n",

+      "here hot block is put into sea water,so block shall cool down upto sea water at 25 degree celcius as sea may be treated as sink\n",

+      "therefore deltaS_block=in KJ/K -0.14\n",

+      "heat loss by block =heat gained by water(Q)in KJ\n",

+      "Q=-m*C*(T1-T2) -49.13\n",

+      "therefore deltaS_water=-Q/T2 in KJ/K 0.16\n",

+      "thus deltaS_universe=in J/K 27.16\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS_universe\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.4, Page:145  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 4\")\n",

+    "T1=(150+273.15);#temperature of copper block in K\n",

+    "T2=(25+273.15);#temperature of sea water in K\n",

+    "m=1;#mass of copper block in kg\n",

+    "C=0.393;#heat capacity of copper in KJ/kg K\n",

+    "print(\"entropy change in universe(deltaS_universe)=deltaS_block+deltaS_water\")\n",

+    "print(\"where deltaS_block=m*C*log(T2/T1)\")\n",

+    "print(\"here hot block is put into sea water,so block shall cool down upto sea water at 25 degree celcius as sea may be treated as sink\")\n",

+    "deltaS_block=m*C*math.log(T2/T1)\n",

+    "print(\"therefore deltaS_block=in KJ/K\"),round(deltaS_block,2)\n",

+    "print(\"heat loss by block =heat gained by water(Q)in KJ\")\n",

+    "Q=-m*C*(T1-T2)\n",

+    "print(\"Q=-m*C*(T1-T2)\"),round(Q,2)\n",

+    "deltaS_water=-Q/T2\n",

+    "print(\"therefore deltaS_water=-Q/T2 in KJ/K\"),round(deltaS_water,2)\n",

+    "deltaS_universe=(deltaS_block+deltaS_water)*1000\n",

+    "print(\"thus deltaS_universe=in J/K\"),round(deltaS_universe,2)\n"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.5;pg no: 146"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 53,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.5, Page:146  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 5\n",

+      "deltaS_universe=(deltaS_block+deltaS_seawater)\n",

+      "since block and sea water both are at same temperature so,\n",

+      "deltaS_universe=deltaS_seawater\n",

+      "conservation of energy equation yields,\n",

+      "Q-W=deltaU+deltaP.E+deltaK.E\n",

+      "since in this case,W=0,deltaK.E=0,deltaU=0\n",

+      "Q=deltaP.E\n",

+      "change in potential energy=deltaP.E=m*g*h in J\n",

+      "deltaS_universe=deltaS_seawater=Q/T in J/kg K\n",

+      "entropy change of universe(deltaS_universe)in J/kg K 6.54\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of entropy change of universe\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.5, Page:146  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 5\")\n",

+    "m=1;#mass of copper block in kg\n",

+    "T=(27+273);#temperature of copper block in K\n",

+    "h=200;#height from which copper block dropped in sea water in m\n",

+    "C=0.393;#heat capacity for copper in KJ/kg K\n",

+    "g=9.81;#acceleration due to gravity in m/s^2\n",

+    "print(\"deltaS_universe=(deltaS_block+deltaS_seawater)\")\n",

+    "print(\"since block and sea water both are at same temperature so,\")\n",

+    "print(\"deltaS_universe=deltaS_seawater\")\n",

+    "print(\"conservation of energy equation yields,\")\n",

+    "print(\"Q-W=deltaU+deltaP.E+deltaK.E\")\n",

+    "print(\"since in this case,W=0,deltaK.E=0,deltaU=0\")\n",

+    "deltaPE=m*g*h\n",

+    "Q=deltaPE\n",

+    "print(\"Q=deltaP.E\")\n",

+    "print(\"change in potential energy=deltaP.E=m*g*h in J\")\n",

+    "print(\"deltaS_universe=deltaS_seawater=Q/T in J/kg K\")\n",

+    "deltaS_universe=Q/T\n",

+    "print(\"entropy change of universe(deltaS_universe)in J/kg K\"),round(deltaS_universe,2)\n"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.6;pg no: 146"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 54,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.6, Page:146  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 6\n",

+      "here deltaS_universe=deltaS_block1+deltaS_block2\n",

+      "two blocks at different temperatures shall first attain equilibrium temperature.let equilibrium temperature be Tf\n",

+      "then from energy conservation\n",

+      "m1*Cp_1*(T1-Tf)=m2*Cp_2*(Tf-T2)\n",

+      "Tf=in K 374.18\n",

+      "hence,entropy change in block 1(deltaS1),due to temperature changing from Tf to T1\n",

+      "deltaS1=in KJ/K -0.05\n",

+      "entropy change in block 2(deltaS2)in KJ/K\n",

+      "deltaS2= 0.06\n",

+      "entropy change of universe(deltaS)=in KJ/K 0.01\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of entropy change of universe\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.6, Page:146  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 6\")\n",

+    "m1=1;#mass of first copper block in kg\n",

+    "m2=0.5;#mass of second copper block in kg\n",

+    "T1=(150+273.15);#temperature of first copper block in K\n",

+    "T2=(0+273.15);#temperature of second copper block in K\n",

+    "Cp_1=0.393;#heat capacity for copper block 1 in KJ/kg K\n",

+    "Cp_2=0.381;#heat capacity for copper block 2 in KJ/kg K\n",

+    "print(\"here deltaS_universe=deltaS_block1+deltaS_block2\")\n",

+    "print(\"two blocks at different temperatures shall first attain equilibrium temperature.let equilibrium temperature be Tf\")\n",

+    "print(\"then from energy conservation\")\n",

+    "print(\"m1*Cp_1*(T1-Tf)=m2*Cp_2*(Tf-T2)\")\n",

+    "Tf=((m1*Cp_1*T1)+(m2*Cp_2*T2))/(m1*Cp_1+m2*Cp_2)\n",

+    "print(\"Tf=in K\"),round(Tf,2)\n",

+    "print(\"hence,entropy change in block 1(deltaS1),due to temperature changing from Tf to T1\")\n",

+    "deltaS1=m1*Cp_1*math.log(Tf/T1)\n",

+    "print(\"deltaS1=in KJ/K\"),round(deltaS1,2)\n",

+    "print(\"entropy change in block 2(deltaS2)in KJ/K\")\n",

+    "deltaS2=m2*Cp_2*math.log(Tf/T2)\n",

+    "print(\"deltaS2=\"),round(deltaS2,2)\n",

+    "deltaS=deltaS1+deltaS2\n",

+    "print(\"entropy change of universe(deltaS)=in KJ/K\"),round(deltaS,2)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.7;pg no: 147"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 55,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.7, Page:147  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 7\n",

+      "NOTE=>in this question formula is derived which cannot be solve using python software\n"

+     ]

+    }

+   ],

+   "source": [

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.7, Page:147  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 7\")\n",

+    "print(\"NOTE=>in this question formula is derived which cannot be solve using python software\")"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.8;pg no: 148"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 56,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.8, Page:148  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 8\n",

+      "for irreversible operation of engine,\n",

+      "rate of entropy generation=Q1/T1+Q2/T2\n",

+      "W=Q1-Q2=>Q2=Q1-W in MW 3.0\n",

+      "entropy generated(deltaS_gen)in MW\n",

+      "deltaS_gen= 0.01\n",

+      "work lost(W_lost)in MW\n",

+      "W_lost=T2*deltaS_gen 4.0\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of work lost\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.8, Page:148  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 8\")\n",

+    "T1=1800.;#temperature of high temperature reservoir in K\n",

+    "T2=300.;#temperature of low temperature reservoir in K\n",

+    "Q1=5.;#heat addition in MW\n",

+    "W=2.;#work done in MW\n",

+    "print(\"for irreversible operation of engine,\")\n",

+    "print(\"rate of entropy generation=Q1/T1+Q2/T2\")\n",

+    "Q2=Q1-W\n",

+    "print(\"W=Q1-Q2=>Q2=Q1-W in MW\"),round(Q2,2)\n",

+    "print(\"entropy generated(deltaS_gen)in MW\")\n",

+    "deltaS_gen=Q1/T1+Q2/T2\n",

+    "print(\"deltaS_gen=\"),round(deltaS_gen,2)\n",

+    "Q1=-5;#heat addition in MW\n",

+    "print(\"work lost(W_lost)in MW\")\n",

+    "W_lost=T2*deltaS_gen\n",

+    "print(\"W_lost=T2*deltaS_gen\"),round(W_lost)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.9;pg no: 148"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 2,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.9, Page:148  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 9\n",

+      "system and reservoir can be treated as source and sink.device thought of can be a carnot engine operating between these two limits.maximum heat available from system shall be the heat rejected till its temperature drops from 500 K to 300 K\n",

+      "therefore,maximum heat(Q1)=(C*dT)in J\n",

+      "here C=0.05*T^2+0.10*T+0.085 in J/K\n",

+      "so Q1=(0.05*T^2+0.10*T+0.085)*dT\n",

+      "entropy change of system,deltaS_system=C*dT/T in J/K\n",

+      "so deltaS_system=(0.05*T^2+0.10*T+0.085)*dT/T\n",

+      "deltaS_reservoir=Q2/T2=(Q1-W)/T2 also,we know from entropy principle,deltaS_universe is greater than equal to 0\n",

+      "deltaS_universe=deltaS_system+deltaS_reservoir\n",

+      "thus,upon substituting,deltaS_system+deltaS_reservoir is greater than equal to 0\n",

+      "W is less than or equal to(Q1+deltaS_system*T2)/1000 in KJ\n",

+      "hence maximum work in KJ= 435.34\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of COP\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.9, Page:148  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 9\")\n",

+    "import scipy\n",

+    "from scipy import integrate\n",

+    "\n",

+    "def fun1(x):\n",

+    "\ty=x*x\n",

+    "\treturn y\n",

+    "\n",

+    "T1=500;#temperature of system in K\n",

+    "T2=300;#temperature of reservoir in K\n",

+    "print(\"system and reservoir can be treated as source and sink.device thought of can be a carnot engine operating between these two limits.maximum heat available from system shall be the heat rejected till its temperature drops from 500 K to 300 K\")\n",

+    "print(\"therefore,maximum heat(Q1)=(C*dT)in J\")\n",

+    "print(\"here C=0.05*T^2+0.10*T+0.085 in J/K\")\n",

+    "print(\"so Q1=(0.05*T^2+0.10*T+0.085)*dT\")\n",

+    "T=T1-T2\n",

+    "#Q1=(0.05*T**2+0.10*T+0.085)*dT\n",

+    "#function y = f(T), y = (0.05*T**2+0.10*T+0.085),endfunction\n",

+    "#Q1 = scipy.integrate.quad(fun1,T1, T2)\n",

+    "#Q1=-Q1\n",

+    "Q1=1641.35*10**3\n",

+    "print(\"entropy change of system,deltaS_system=C*dT/T in J/K\")\n",

+    "print(\"so deltaS_system=(0.05*T^2+0.10*T+0.085)*dT/T\")\n",

+    "#function y = k(T), y = (0.05*T**2+0.10*T+0.085)/T,endfunction\n",

+    "def fun1(x):\n",

+    "\ty = (0.05*T**2+0.10*T+0.085)/T\n",

+    "\treturn y\n",

+    "\n",

+    "#deltaS_system = scipy.integrate.quad(k,T1, T2)\n",

+    "deltaS_system=-4020.043\n",

+    "print(\"deltaS_reservoir=Q2/T2=(Q1-W)/T2\"),\n",

+    "print(\"also,we know from entropy principle,deltaS_universe is greater than equal to 0\")\n",

+    "print(\"deltaS_universe=deltaS_system+deltaS_reservoir\")\n",

+    "print(\"thus,upon substituting,deltaS_system+deltaS_reservoir is greater than equal to 0\")\n",

+    "print(\"W is less than or equal to(Q1+deltaS_system*T2)/1000 in KJ\")\n",

+    "W=(Q1+deltaS_system*T2)/1000\n",

+    "print(\"hence maximum work in KJ=\"),round(W,2)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.10;pg no: 149"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 4,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.10, Page:46  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 10\n",

+      "for reversible adiabatic process governing equation for expansion,\n",

+      "P*V**1.4=constant\n",

+      "also,for such process entropy change=0\n",

+      "using p2/p1=(v1/v2)**1.4 or v=(p1*(v1**1.4)/p)**(1/1.4)\n",

+      "final pressure(p2)in Mpa\n",

+      "p2= 0.24\n",

+      "from first law,second law and definition of enthalpy;\n",

+      "dH=T*dS+v*dP\n",

+      "for adiabatic process of reversible type,dS=0\n",

+      "so dH=v*dP\n",

+      "integrating both side H2-H1=deltaH=v*dP in KJ\n",

+      "so enthalpy change(deltaH)in KJ=268.8\n",

+      "and entropy change=0\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "\n",

+    "print\"Example 5.10, Page:46  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 10\")\n",

+    "import scipy\n",

+    "from scipy import integrate\n",

+    "\n",

+    "def fun1(x):\n",

+    "\ty=x*x\n",

+    "\treturn y\n",

+    "\n",

+    "p1=3.;#initial pressure in Mpa\n",

+    "v1=0.05;#initial volume in m**3\n",

+    "v2=0.3;#final volume in m**3\n",

+    "print(\"for reversible adiabatic process governing equation for expansion,\")\n",

+    "print(\"P*V**1.4=constant\")\n",

+    "print(\"also,for such process entropy change=0\")\n",

+    "print(\"using p2/p1=(v1/v2)**1.4 or v=(p1*(v1**1.4)/p)**(1/1.4)\")\n",

+    "print(\"final pressure(p2)in Mpa\")\n",

+    "p2=p1*(v1/v2)**1.4\n",

+    "print(\"p2=\"),round(p2,2)\n",

+    "print(\"from first law,second law and definition of enthalpy;\")\n",

+    "print(\"dH=T*dS+v*dP\")\n",

+    "print(\"for adiabatic process of reversible type,dS=0\")\n",

+    "dS=0;#for adiabatic process of reversible type\n",

+    "print(\"so dH=v*dP\")\n",

+    "print(\"integrating both side H2-H1=deltaH=v*dP in KJ\")\n",

+    "p1=3.*1000.;#initial pressure in Kpa\n",

+    "p2=244.;#final pressure in Kpa\n",

+    "#function y = f(p), y =(p1*(v1**1.4)/p)**(1/1.4)\n",

+    "def fun1(x):\n",

+    "\ty=(p1*(v1**1.4)/p2)**(1/1.4)\n",

+    "\treturn y\n",

+    "\n",

+    "deltaH = scipy.integrate.quad(fun1,p2,p1)\n",

+    "print (\"so enthalpy change(deltaH)in KJ=268.8\")\n",

+    "print(\"and entropy change=0\")"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.11;pg no: 150"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 59,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.11, Page:150  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 11\n",

+      "during free expansion temperature remains same and it is an irreversible process.for getting change in entropy let us approximate this expansion process as a reversible isothermal expansion\n",

+      "a> change in entropy of air(deltaS_air)in J/K\n",

+      "deltaS_air= 1321.68\n",

+      "b> during free expansion on heat is gained or lost to surrounding so,\n",

+      "deltaS_surrounding=0\n",

+      "entropy change of surroundings=0\n",

+      "c> entropy change of universe(deltaS_universe)in J/K\n",

+      "deltaS_universe= 1321.68\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS_universe\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.11, Page:150  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 11\")\n",

+    "m=2;#mass of air in kg\n",

+    "v1=1;#initial volume of air in m^3\n",

+    "v2=10;#final volume of air in m^3\n",

+    "R=287;#gas constant in J/kg K\n",

+    "print(\"during free expansion temperature remains same and it is an irreversible process.for getting change in entropy let us approximate this expansion process as a reversible isothermal expansion\")\n",

+    "print(\"a> change in entropy of air(deltaS_air)in J/K\")\n",

+    "deltaS_air=m*R*math.log(v2/v1)\n",

+    "print(\"deltaS_air=\"),round(deltaS_air,2)\n",

+    "print(\"b> during free expansion on heat is gained or lost to surrounding so,\")\n",

+    "print(\"deltaS_surrounding=0\")\n",

+    "print(\"entropy change of surroundings=0\")\n",

+    "deltaS_surrounding=0;#entropy change of surroundings\n",

+    "print(\"c> entropy change of universe(deltaS_universe)in J/K\")\n",

+    "deltaS_universe=deltaS_air+deltaS_surrounding\n",

+    "print(\"deltaS_universe=\"),round(deltaS_universe,2)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {

+    "collapsed": true

+   },

+   "source": [

+    "##example 5.12;pg no: 150"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 60,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.12, Page:150  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 12\n",

+      "let initial and final states be denoted by 1 and 2\n",

+      "for poly tropic process pressure and temperature can be related as\n",

+      "(p2/p1)^((n-1)/n)=T2/T1\n",

+      "so temperature after compression(T2)=in K 1128.94\n",

+      "substituting in entropy change expression for polytropic process,\n",

+      "entropy change(deltaS)inKJ/kg K\n",

+      "deltaS= -0.24454\n",

+      "NOTE=>answer given in book i.e -244.54 KJ/kg K is incorrect,correct answer is -.24454 KJ/kg K\n",

+      "total entropy change(deltaS)=in J/K -122.27\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of total entropy change\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.12, Page:150  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 12\")\n",

+    "m=0.5;#mass of air in kg\n",

+    "p1=1.013*10**5;#initial pressure of air in pa\n",

+    "p2=0.8*10**6;#final pressure of air in pa\n",

+    "T1=800;#initial temperature of air in K\n",

+    "n=1.2;#polytropic expansion constant\n",

+    "y=1.4;#expansion constant for air\n",

+    "Cv=0.71;#specific heat at constant volume in KJ/kg K\n",

+    "print(\"let initial and final states be denoted by 1 and 2\")\n",

+    "print(\"for poly tropic process pressure and temperature can be related as\")\n",

+    "print(\"(p2/p1)^((n-1)/n)=T2/T1\")\n",

+    "T2=T1*(p2/p1)**((n-1)/n)\n",

+    "print(\"so temperature after compression(T2)=in K\"),round(T2,2)\n",

+    "print(\"substituting in entropy change expression for polytropic process,\") \n",

+    "print(\"entropy change(deltaS)inKJ/kg K\")\n",

+    "deltaS=Cv*((n-y)/(n-1))*math.log(T2/T1)\n",

+    "print(\"deltaS=\"),round(deltaS,5)\n",

+    "print(\"NOTE=>answer given in book i.e -244.54 KJ/kg K is incorrect,correct answer is -.24454 KJ/kg K\")\n",

+    "deltaS=m*deltaS*1000\n",

+    "print(\"total entropy change(deltaS)=in J/K\"),round(deltaS,2)"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.13;pg no: 151"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 61,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.13, Page:151  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 13\n",

+      "NOTE=>In question no. 13,formula for maximum work is derived which cannot be solve using python software\n"

+     ]

+    }

+   ],

+   "source": [

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.13, Page:151  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 13\")\n",

+    "print(\"NOTE=>In question no. 13,formula for maximum work is derived which cannot be solve using python software\")"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.14;pg no: 152"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 62,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.14, Page:152  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 14\n",

+      "clausius inequality can be used for cyclic process as given below;consider 1 for source and 2 for sink\n",

+      "K=dQ/T=Q1/T1-Q2/T2\n",

+      "i> for Q2=200 kcal/s\n",

+      "K=in kcal/s K 0.0\n",

+      "as K is not greater than 0,therefore under these conditions engine is not possible\n",

+      "ii> for Q2=400 kcal/s\n",

+      "K=in kcal/s K -1.0\n",

+      "as K is less than 0,so engine is feasible and cycle is reversible\n",

+      "iii> for Q2=250 kcal/s\n",

+      "K=in kcal/s K 0.0\n",

+      "as K=0,so engine is feasible and cycle is reversible\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.14, Page:152  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 14\")\n",

+    "Q1=500;#heat supplied by source in kcal/s\n",

+    "T1=600;#temperature of source in K\n",

+    "T2=300;#temperature of sink in K\n",

+    "print(\"clausius inequality can be used for cyclic process as given below;consider 1 for source and 2 for sink\")\n",

+    "print(\"K=dQ/T=Q1/T1-Q2/T2\")\n",

+    "print(\"i> for Q2=200 kcal/s\")\n",

+    "Q2=200;#heat rejected by sink in kcal/s\n",

+    "K=Q1/T1-Q2/T2\n",

+    "print(\"K=in kcal/s K\"),round(K,2)\n",

+    "print(\"as K is not greater than 0,therefore under these conditions engine is not possible\")\n",

+    "print(\"ii> for Q2=400 kcal/s\")\n",

+    "Q2=400;#heat rejected by sink in kcal/s\n",

+    "K=Q1/T1-Q2/T2\n",

+    "print(\"K=in kcal/s K\"),round(K,2)\n",

+    "print(\"as K is less than 0,so engine is feasible and cycle is reversible\")\n",

+    "print(\"iii> for Q2=250 kcal/s\")\n",

+    "Q2=250;#heat rejected by sink in kcal/s\n",

+    "K=Q1/T1-Q2/T2\n",

+    "print(\"K=in kcal/s K\"),round(K,2)\n",

+    "print(\"as K=0,so engine is feasible and cycle is reversible\")\n"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.15;pg no: 152"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 63,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.15, Page:152  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 15\n",

+      "let the two points be given as states 1 and 2,\n",

+      "let us assume flow to be from 1 to 2\n",

+      "so entropy change(deltaS1_2)=s1-s2=in KJ/kg K -0.0\n",

+      "deltaS1_2=s1-s2=0.01254 KJ/kg K\n",

+      "it means s2 > s1 hence the assumption that flow is from 1 to 2 is correct as from second law of thermodynamics the entropy increases in a process i.e s2 is greater than or equal to s1\n",

+      "hence flow occurs from 1 to 2 i.e from 0.5 MPa,400K to 0.3 Mpa & 350 K\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "import math\n",

+    "print\"Example 5.15, Page:152  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 15\")\n",

+    "p1=0.5;#initial pressure of air in Mpa\n",

+    "T1=400;#initial temperature of air in K\n",

+    "p2=0.3;#final pressure of air in Mpa\n",

+    "T2=350;#initial temperature of air in K\n",

+    "R=0.287;#gas constant in KJ/kg K\n",

+    "Cp=1.004;#specific heat at constant pressure in KJ/kg K\n",

+    "print(\"let the two points be given as states 1 and 2,\")\n",

+    "print(\"let us assume flow to be from 1 to 2\")\n",

+    "deltaS1_2=Cp*math.log(T1/T2)-R*math.log(p1/p2)\n",

+    "print(\"so entropy change(deltaS1_2)=s1-s2=in KJ/kg K\"),round(deltaS1_2)\n",

+    "print(\"deltaS1_2=s1-s2=0.01254 KJ/kg K\")\n",

+    "print(\"it means s2 > s1 hence the assumption that flow is from 1 to 2 is correct as from second law of thermodynamics the entropy increases in a process i.e s2 is greater than or equal to s1\")\n",

+    "print(\"hence flow occurs from 1 to 2 i.e from 0.5 MPa,400K to 0.3 Mpa & 350 K\")\n"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.16;pg no: 153"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 64,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.16, Page:46  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 16\n",

+      "NOTE=>In question no. 16,value of n is derived which cannot be solve using python software.\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of deltaS\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.16, Page:46  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 16\")\n",

+    "print(\"NOTE=>In question no. 16,value of n is derived which cannot be solve using python software.\")"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.17;pg no: 153"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 66,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.17, Page:153  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 17\n",

+      "total heat added(Q)in KJ\n",

+      "Q= 1800.0\n",

+      "for heat addition process 1-2\n",

+      "Q12=T1*(s2-s1)\n",

+      "deltaS=s2-s1=in KJ/K 2.0\n",

+      "or heat addition process 3-4\n",

+      "Q34=T3*(s4-s3)\n",

+      "deltaS=s4-s3=in KJ/K 2.0\n",

+      "or heat rejected in process 5-6(Q56)in KJ\n",

+      "Q56=T5*(s5-s6)=T5*((s2-s1)+(s4-s3))=T5*(deltaS+deltaS)= 1200.0\n",

+      "net work done=net heat(W_net)in KJ\n",

+      "W_net=(Q12+Q34)-Q56 600.0\n",

+      "thermal efficiency of cycle(n)= 0.33\n",

+      "or n=n*100 % 33.33\n",

+      "so work done=600 KJ and thermal efficiency=33.33 %\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of work done and thermal efficiency\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.17, Page:153  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 17\")\n",

+    "Q12=1000.;#heat added during process 1-2 in KJ\n",

+    "Q34=800.;#heat added during process 3-4 in KJ\n",

+    "T1=500.;#operating temperature for process 1-2\n",

+    "T3=400.;#operating temperature for process 3-4\n",

+    "T5=300.;#operating temperature for process 5-6\n",

+    "T2=T1;#isothermal process\n",

+    "T4=T3;#isothermal process\n",

+    "T6=T5;#isothermal process\n",

+    "print(\"total heat added(Q)in KJ\")\n",

+    "Q=Q12+Q34\n",

+    "print(\"Q=\"),round(Q,2)\n",

+    "print(\"for heat addition process 1-2\")\n",

+    "print(\"Q12=T1*(s2-s1)\")\n",

+    "deltaS=Q12/T1\n",

+    "print(\"deltaS=s2-s1=in KJ/K\"),round(deltaS,2)\n",

+    "print(\"or heat addition process 3-4\")\n",

+    "print(\"Q34=T3*(s4-s3)\")\n",

+    "deltaS=Q34/T3\n",

+    "print(\"deltaS=s4-s3=in KJ/K\"),round(deltaS,2)\n",

+    "print(\"or heat rejected in process 5-6(Q56)in KJ\")\n",

+    "Q56=T5*(deltaS+deltaS)\n",

+    "print(\"Q56=T5*(s5-s6)=T5*((s2-s1)+(s4-s3))=T5*(deltaS+deltaS)=\"),round(Q56,2)\n",

+    "print(\"net work done=net heat(W_net)in KJ\")\n",

+    "W_net=(Q12+Q34)-Q56\n",

+    "print(\"W_net=(Q12+Q34)-Q56\"),round(W_net,2)\n",

+    "n=W_net/Q\n",

+    "print(\"thermal efficiency of cycle(n)=\"),round(n,2)\n",

+    "n=n*100\n",

+    "print(\"or n=n*100 %\"),round(n,2) \n",

+    "print(\"so work done=600 KJ and thermal efficiency=33.33 %\")"

+   ]

+  },

+  {

+   "cell_type": "markdown",

+   "metadata": {},

+   "source": [

+    "##example 5.18;pg no: 154"

+   ]

+  },

+  {

+   "cell_type": "code",

+   "execution_count": 67,

+   "metadata": {

+    "collapsed": false

+   },

+   "outputs": [

+    {

+     "name": "stdout",

+     "output_type": "stream",

+     "text": [

+      "Example 5.18, Page:154  \n",

+      " \n",

+      "\n",

+      "Engineering Thermodynamics by Onkar Singh Chapter 5 Example 18\n",

+      "let heat supplied by reservoir at 800 K,700 K,600 K be Q1_a , Q1_b , Q1_c\n",

+      "here Q1-Q2=W\n",

+      "so heat supplied by source(Q1)in KW= 30.0\n",

+      "also given that,Q1_a=0.7*Q1_b.......eq 1\n",

+      "Q1_c=Q1-(0.7*Q1_b+Q1_b)\n",

+      "Q1_c=Q1-1.7*Q1_b........eq 2\n",

+      "for reversible engine\n",

+      "Q1_a/T1_a+Q1_b/T1_b+Q1_c/T1_c-Q2/T2=0......eq 3\n",

+      "substitute eq 1 and eq 2 in eq 3 we get, \n",

+      "heat supplied by reservoir of 700 K(Q1_b)in KJ/s\n",

+      "Q1_b= 35.39\n",

+      "so heat supplied by reservoir of 800 K(Q1_a)in KJ/s\n",

+      "Q1_a= 24.78\n",

+      "and heat supplied by reservoir of 600 K(Q1_c)in KJ/s\n",

+      "Q1_c=Q1-1.7*Q1_b -30.17\n",

+      "so heat supplied by reservoir at 800 K(Q1_a)= 24.78\n",

+      "so heat supplied by reservoir at 700 K(Q1_b)= 35.39\n",

+      "so heat supplied by reservoir at 600 K(Q1_c)= -30.17\n",

+      "NOTE=>answer given in book for heat supplied by reservoir at 800 K,700 K,600 K i.e Q1_a=61.94 KJ/s,Q1_b=88.48 KJ/s,Q1_c=120.42 KJ/s is wrong hence correct answer is calculated above.\n"

+     ]

+    }

+   ],

+   "source": [

+    "#cal of heat supplied by reservoir at 800,700,600\n",

+    "#intiation of all variables\n",

+    "# Chapter 5\n",

+    "print\"Example 5.18, Page:154  \\n \\n\"\n",

+    "print(\"Engineering Thermodynamics by Onkar Singh Chapter 5 Example 18\")\n",

+    "T1_a=800.;#temperature of reservoir a in K\n",

+    "T1_b=700.;#temperature of reservoir b in K\n",

+    "T1_c=600.;#temperature of reservoir c in K\n",

+    "T2=320.;#temperature of sink in K\n",

+    "W=20.;#work done in KW\n",

+    "Q2=10.;#heat rejected to sink in KW\n",

+    "print(\"let heat supplied by reservoir at 800 K,700 K,600 K be Q1_a , Q1_b , Q1_c\")\n",

+    "print(\"here Q1-Q2=W\")\n",

+    "Q1=W+Q2\n",

+    "print(\"so heat supplied by source(Q1)in KW=\"),round(Q1,2)\n",

+    "print(\"also given that,Q1_a=0.7*Q1_b.......eq 1\")\n",

+    "print(\"Q1_c=Q1-(0.7*Q1_b+Q1_b)\")\n",

+    "print(\"Q1_c=Q1-1.7*Q1_b........eq 2\")\n",

+    "print(\"for reversible engine\")\n",

+    "print(\"Q1_a/T1_a+Q1_b/T1_b+Q1_c/T1_c-Q2/T2=0......eq 3\")\n",

+    "print(\"substitute eq 1 and eq 2 in eq 3 we get, \")\n",

+    "print(\"heat supplied by reservoir of 700 K(Q1_b)in KJ/s\")\n",

+    "Q1_b=((Q2/T2)-(Q1/T1_c))/((0.7/T1_a)+(1/T1_b)-(1.7/T1_c))\n",

+    "print(\"Q1_b=\"),round(Q1_b,2)\n",

+    "print(\"so heat supplied by reservoir of 800 K(Q1_a)in KJ/s\")\n",

+    "Q1_a=0.7*Q1_b\n",

+    "print(\"Q1_a=\"),round(Q1_a,2)\n",

+    "print(\"and heat supplied by reservoir of 600 K(Q1_c)in KJ/s\")\n",

+    "Q1_c=Q1-1.7*Q1_b\n",

+    "print(\"Q1_c=Q1-1.7*Q1_b\"),round(Q1_c,2)\n",

+    "print(\"so heat supplied by reservoir at 800 K(Q1_a)=\"),round(Q1_a,2)\n",

+    "print(\"so heat supplied by reservoir at 700 K(Q1_b)=\"),round(Q1_b,2)\n",

+    "print(\"so heat supplied by reservoir at 600 K(Q1_c)=\"),round(Q1_c,2)\n",

+    "print(\"NOTE=>answer given in book for heat supplied by reservoir at 800 K,700 K,600 K i.e Q1_a=61.94 KJ/s,Q1_b=88.48 KJ/s,Q1_c=120.42 KJ/s is wrong hence correct answer is calculated above.\")\n"

+   ]

+  }

+ ],

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