Effect of guest-dependent reference hydrate vapor pressure in thermodynamic modeling of gas hydrate phase equilibria, with various combinations of equations of state and activity coefficient models

被引:8
作者
Anil, Jugal N. [1 ]
Bhawangirkar, Dnyaneshwar R. [2 ]
Sangwai, Jitendra S. [1 ]
机构
[1] Indian Inst Technol Madras, Dept Chem Engn, Chennai 600036, Tamil Nadu, India
[2] Indian Inst Technol, Dept Chem Engn, Mumbai 400076, Maharashtra, India
关键词
Activity coefficient model; Equation of state; Gas hydrate; Phase equilibria; Thermodynamic model; TBAB PLUS NACL; CARBON-DIOXIDE; CLATHRATE HYDRATE; METHANE HYDRATE; DISSOCIATION PRESSURES; STABILITY CONDITIONS; AQUEOUS-SOLUTIONS; NATURAL GASES; OF-STATE; PREDICTION;
D O I
10.1016/j.fluid.2021.113356
中图分类号
O414.1 [热力学];
学科分类号
摘要
Using the van der Waals solid solution theory and the fugacity-based approach of Klauda and Sandler, a thermodynamic model to predict the phase equilibria of gas hydrates using an Equation of State (EOS) and an Activity Coefficient Model (ACM) is presented. Here, we have studied five EOS models, that are, Peng-Robinson-Stryjek-Vera (PRSV), Patel-Teja (PT), Soave-Redlich-Kwong (SRK), Peng-Robinson (PR), and Redlich-Kwong (RK) to calculate the gas phase fugacity and four ACMs, that are, modified UNIFAC (mU-NIFAC), UNIQUAC, Wilson and NRTL to model the liquid phase non-ideality. The Wilson and NRTL activity coefficient models have previously been used for systems containing additional chemicals in the liquid phase but not for pure water in coexistence with gas hydrates, to the best of our knowledge, and this has been explored in this work. By making the empty hydrate vapor pressure parameters guest dependent, the model improves upon the predictions from our previous model for sI and sII hydrates significantly and has drastically reduced the errors especially in modeling sII hydrates. The best combinations of EOS and ACM in L-H-V equilibrium and best EOS for I-H-V equilibrium, respectively, for each compound, to be used in the guest dependent model from the 100 combinations of EOS and ACM (for L-H-V equilibrium) and 25 possible EOS options (for I-H-V equilibrium) examined are: RK-mUNIFAC and SRK for CH4, RK-mUNIFAC and PRSV for CO2, RK-mUNIFAC and PR for C2H6, SRK-mUNIFAC and SRK for N-2, and PR-NRTL and RK for C3H8. While different EOS work well for CH4, CO2, C2H6 and C3H8 hydrates in L-H-V and IH-V equilibria, the SRK EOS works well for N-2 hydrates in both L-H-V and I-H-V equilibria. We have also reported the solubilities of guest species in liquid water in equilibrium with hydrates and the hydrate cage occupancies from the models producing the least error as data on these facets is limited. (C) 2021 Elsevier B.V. All rights reserved.
引用
收藏
页数:15
相关论文
共 85 条
  • [1] STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS
    ABRAMS, DS
    PRAUSNITZ, JM
    [J]. AICHE JOURNAL, 1975, 21 (01) : 116 - 128
  • [2] HYDRATES OF CARBON-DIOXIDE AND METHANE MIXTURES
    ADISASMITO, S
    FRANK, RJ
    SLOAN, ED
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1991, 36 (01) : 68 - 71
  • [3] Experimental determination and thermodynamic modeling of clathrate hydrate stability conditions in methane plus hydrogen sulfide plus water system
    Aghajanloo, Mahnaz
    Taheri, Zahra
    Behbahani, Taraneh Jafari
    Mohammadi, Amir H.
    Ehsani, Mohammad Reza
    Heydarian, Hamed
    [J]. JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2020, 83
  • [4] A robust model for the phase stability of clathrate hydrate of methane in an aqueous systems of TBAB, TBAB plus NaCl and THF suitable for storage and transportation of natural gas
    Avula, Venkata Ramana
    Gardas, Ramesh L.
    Sangwai, Jitendra S.
    [J]. JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2016, 33 : 509 - 517
  • [5] An efficient model for the prediction of CO2 hydrate phase stability conditions in the presence of inhibitors and their mixtures
    Avula, Venkata Ramana
    Gardas, Ramesh L.
    Sangwai, Jitendra S.
    [J]. JOURNAL OF CHEMICAL THERMODYNAMICS, 2015, 85 : 163 - 170
  • [6] An improved model for the phase equilibrium of methane hydrate inhibition in the presence of ionic liquids
    Avula, Venkata Ramana
    Gardas, Ramesh L.
    Sangwai, Jitendra S.
    [J]. FLUID PHASE EQUILIBRIA, 2014, 382 : 187 - 196
  • [7] The next generation of hydrate prediction I. Hydrate standard states and incorporation of spectroscopy
    Ballard, AL
    Sloan, ED
    [J]. FLUID PHASE EQUILIBRIA, 2002, 194 : 371 - 383
  • [8] Gas Hydrate Structure and Pressure Predictions Based on an Updated Fugacity-Based Model with the PSRK Equation of State
    Bandyopadhyay, Arpan A.
    Klauda, Jeffery B.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (01) : 148 - 157
  • [9] Prediction of phase stability conditions of gas hydrates of methane and carbon dioxide in porous media
    Barmavath, Tejaswi
    Mekala, Prathyusha
    Sangwai, Jitendra S.
    [J]. JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2014, 18 : 254 - 262
  • [10] Bhawangirkar Dnyaneshwar R., 2021, Proceedings of the Fifth International Conference in Ocean Engineering (ICOE2019). Lecture Notes in Civil Engineering (LNCE 106), P405, DOI 10.1007/978-981-15-8506-7_34