├── .gitignore ├── README.md ├── contents ├── cheat-sheets │ └── tuple-list-and-array-operations.ipynb ├── external-references │ └── _2 ├── featured-assignments │ └── TPQB-UFRJ-2016.3 │ │ ├── Adriana-Teixeira │ │ ├── Dados de Psat - agua.txt │ │ ├── Dados de Psat - etanol.txt │ │ ├── Etanol liquido 200 oC.txt │ │ ├── Etanol vapor 200 oC.txt │ │ ├── Hexcesso 323,15K 0,04MPa.txt │ │ ├── Trabalho de Termodinamica Aplicada - Adriana - Parte 1 - Agua.ipynb │ │ ├── Trabalho de Termodinamica Aplicada - Adriana - Parte 2 - Etanol.ipynb │ │ └── Trabalho de Termodinâmica Aplicada - Adriana - Parte 3 - Mistura.ipynb │ │ ├── André-Clemente-de-Farias │ │ ├── acetone_experimental.txt │ │ ├── ethanol_experimental.txt │ │ ├── mistura.ipynb │ │ ├── puro.ipynb │ │ ├── water_acetone_H_Exc.txt │ │ ├── water_acetone_P1.txt │ │ └── water_experimental.txt │ │ ├── Antonio-Alberto-Ribeiro-Patricio │ │ ├── Dados de Psat - etanol.txt │ │ ├── Dados de Psat - hexano.txt │ │ ├── Etanol liquido 150 oC.txt │ │ ├── Etanol vapor 150 oC.txt │ │ ├── Hexcesso 323K.txt │ │ ├── Teste do Ln Gamma x Temperatura.ipynb │ │ ├── Trabalho de Termodinâmica Aplicada - Antonio Patricio - Parte 1 Rev5.ipynb │ │ ├── Trabalho de Termodinâmica Aplicada - Antonio Patricio - Parte 2 Rev2.ipynb │ │ └── water vapor pressure.txt │ │ ├── Caroline-Santos-Marques │ │ ├── Ethanol_saturation_pressure-C.ipynb │ │ ├── Uniquac_T_SRK.m │ │ ├── dev.m │ │ ├── exp_data_vapor_pressure_ethanol.txt │ │ ├── exp_data_vapor_pressure_water.txt │ │ └── water_saturation_pressure.ipynb │ │ ├── Fabiana-Coelho │ │ ├── P1a.ipynb │ │ ├── P1b.ipynb │ │ ├── P2.ipynb │ │ ├── exp data entropia agua 298.1K.txt │ │ ├── exp data entropia agua 298K.txt │ │ ├── exp data entropia agua 463.1K.txt │ │ ├── exp data entropia agua 485K.txt │ │ ├── exp data vapor pressure acetone.txt │ │ ├── exp data vapor pressure water.txt │ │ ├── exp data volumes 293K.txt │ │ ├── exp data volumes 308K.txt │ │ ├── exp data volumes 323K.txt │ │ ├── exp data volumes 338K.txt │ │ ├── exp data volumes 633K.txt │ │ ├── exp data volumes acetona 348K.txt │ │ ├── exp data volumes acetona 373K.txt │ │ ├── exp data volumes acetona 398K.txt │ │ └── lichtenbelt1985.png │ │ ├── Mariana-Amorim-de-Almeida │ │ ├── AdsorptionEoS.ipynb │ │ └── GA.png │ │ ├── Pedro-Andrade │ │ ├── ELV_Agua_acetona.ipynb │ │ ├── P1.ipynb │ │ ├── Psat_Acetona_exp.ipynb │ │ ├── psat_acet_prog.txt │ │ └── psat_h202.txt │ │ ├── README.md │ │ └── Roberto-Fonseca-Junior │ │ ├── 1.Exercicio termodinamica agua Roberto Fonseca versao final.ipynb │ │ ├── 1.Exercicio termodinamica etanol Roberto Fonseca versao final.ipynb │ │ ├── 2.termodinamica exercicio 2 Roberto Fonseca versao final.ipynb │ │ ├── Dados de Psat - agua.txt │ │ ├── Dados de Psat - etanol.txt │ │ ├── Etanol liquido 150 oC.txt │ │ └── Etanol vapor 150 oC.txt ├── main-lectures │ ├── 1-jupyternotebook-python-1stlaw.ipynb │ ├── 2-numpy-matplotlib-vdW-EoS-isotherms.ipynb │ ├── 3a-VolumeMolar-PressaoDeSaturacao-EquacaoDeEstadoCubica.ipynb │ ├── 3b-scipy-MolarVolume-SaturationPressure-CubicEoS.ipynb │ ├── 4-sympy-vdWEoS-analytical-solutions.ipynb │ ├── GA-1.png │ ├── GA-2.png │ ├── GA-3a.png │ ├── GA-3b.png │ ├── GA-4.png │ ├── GA-GE1.png │ ├── GA-GE2.png │ ├── GA-GE3.png │ ├── GA-GE4.png │ ├── GA-GE5.png │ ├── GA-GE6.png │ ├── GA-HYD1.png │ ├── GE1-NRTL-graphically.ipynb │ ├── GE2-NRTL-linearAlgebra.ipynb │ ├── GE3-VLE-azeotropy.ipynb │ ├── GE4-LLE-flash.ipynb │ ├── GE5-LLE-flash-scipy.ipynb │ ├── GE6-LLE-flash-convergenceAnalysis.ipynb │ ├── HYD1-methane-hydrates.ipynb │ └── support-files │ │ ├── C1-sI-hydrates-HLwGequilibria-expData.txt │ │ └── algorithms.png ├── models-and-algorithms-laboratory │ ├── Aq_modeling │ │ └── Pitzer_NaCl │ │ │ ├── Pitzer_f2pytest.py │ │ │ ├── README.md │ │ │ ├── mPitzer_w_NaCl.f90 │ │ │ └── plot.png │ ├── HYDincipient_LVflash │ │ ├── HYD_flashLV.ipynb │ │ └── README.md │ └── LVE algorithms │ │ └── PxT_L-V_Phase_Envelope_given_z │ │ ├── GA-pxtphaseenv.png │ │ ├── README.md │ │ ├── fortran_library │ │ ├── Makefile │ │ ├── README.txt │ │ ├── bin │ │ │ └── Trace_The_Envelope.so │ │ ├── obj │ │ │ ├── EOS.o │ │ │ ├── GaussElimination.o │ │ │ ├── PhaseEnvelope.o │ │ │ ├── cubic_solver.mod │ │ │ ├── cubic_solver.o │ │ │ ├── eos.mod │ │ │ └── gaussianelimination.mod │ │ ├── sample_input │ │ │ └── input.txt │ │ ├── sample_output │ │ │ ├── output.csv │ │ │ └── plot_template.xls │ │ └── src │ │ │ ├── EOS.f90 │ │ │ ├── GaussElimination.f90 │ │ │ ├── PhaseEnvelope.f90 │ │ │ └── cubic_solver.f90 │ │ ├── fortran_standalone │ │ ├── Makefile │ │ ├── README.txt │ │ ├── bin │ │ │ └── Trace_The_Envelope.elf │ │ ├── input │ │ │ └── input.txt │ │ ├── obj │ │ │ ├── EOS.o │ │ │ ├── GaussElimination.o │ │ │ ├── PhaseEnvelope.o │ │ │ ├── cubic_solver.mod │ │ │ ├── cubic_solver.o │ │ │ ├── eos.mod │ │ │ └── gaussianelimination.mod │ │ ├── output │ │ │ ├── output.csv │ │ │ └── plot_template.xls │ │ └── src │ │ │ ├── EOS.f90 │ │ │ ├── GaussElimination.f90 │ │ │ ├── PhaseEnvelope.f90 │ │ │ └── cubic_solver.f90 │ │ └── ipynb_caller_script_and_plotting_tool │ │ ├── README.md │ │ ├── input │ │ └── input.txt │ │ ├── ipynb_caller_script_and_plotting_tool.ipynb │ │ └── output │ │ └── output.csv ├── texts-library │ ├── Abreu, C. 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