Application of the cell potential method to predict phase equilibria of multicomponent gas hydrate systems

被引:47
|
作者
Anderson, BJ
Bazant, MZ
Tester, JW
Trout, BL
机构
[1] MIT, Dept Chem Engn, Cambridge, MA 02139 USA
[2] MIT, Dept Math, Cambridge, MA 02139 USA
来源
JOURNAL OF PHYSICAL CHEMISTRY B | 2005年 / 109卷 / 16期
关键词
D O I
10.1021/jp045551g
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
We present the application of a mathematical method reported earlier(1) by which the van der Waals-Platteeuw statistical mechanical model with the Lennard-Jones and Devonshire approximation can be posed as an integral equation with the unknown function being the intermolecular potential between the guest molecules and the host molecules. This method allows us to solve for the potential directly for hydrates for which the Langmuir constants are computed, either from experimental data or from ab initio data. Given the assumptions made in the van der Waals-Platteeuw model with the spherical-cell approximation, there are an infinite number of solutions; however, the only solution without cusps is a unique central-well solution in which the potential is at a finite minimum at the center to the cage. From this central-well solution, we have found the potential well depths and volumes of negative energy for 16 single-component hydrate systems: ethane (C2H6), cyclopropane (C3H6), methane (CH4), argon (Ar), and chlorodifluoromethane (R-22) in structure I; and ethane (C2H6), cyclopropane (C3H6), propane (C3H8), isobutane (C4H10), methane (CH4), argon (Ar), trichlorofluoromethane (R-11), dichlorodifluoromethane (R-12), bromotrifluoromethane (R-13B1), chloroform (CHCl3) and 1,1,1,2-tetrafluoroethane (R-134a) in structure II. This method and the calculated cell potentials were validated by predicting existing mixed hydrate phase equilibrium data without any fitting parameters and calculating mixture phase diagrams for methane, ethane, isobutane, and cyclopropane mixtures. Several structural transitions that have been determined experimentally as well as some structural transitions that have not been examined experimentally were also predicted. In the methane-cyclopropane hydrate system, a structural transition from structure I to structure II and back to structure I is predicted to occur outside of the known structure II range for the cyclopropane hydrate. Quintuple (L-w-sI-sII-L-hc-V) points have been predicted for the ethane-propane-water (277.3 K, 12.28 bar, and x(eth,waterfree) = 0.676) and ethane-isobutane-water (274.7 K, 7.18 bar, and X-eth,X-waterfree = 0.81) systems.
引用
收藏
页码:8153 / 8163
页数:11
相关论文
共 50 条
  • [1] Predicting Gas Hydrate Equilibria in Multicomponent Systems with a Machine Learning Approach
    Nasir, Qazi
    Majeed, Wameath S. Abdul S.
    Suleman, Humbul
    CHEMICAL ENGINEERING & TECHNOLOGY, 2023, 46 (09) : 1854 - 1867
  • [2] Advancements in hydrate phase equilibria and modeling of gas hydrates systems
    Khan, M. Naveed
    Warrier, Pramod
    Peters, Cor J.
    Koh, Carolyn A.
    FLUID PHASE EQUILIBRIA, 2018, 463 : 48 - 61
  • [3] PHASE EQUILIBRIA IN MULTICOMPONENT SYSTEMS
    RICCI, JE
    JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1965, 87 (21) : 4981 - &
  • [4] The phase equilibria of multicomponent gas hydrate in methanol/ethylene glycol solution based formation water
    Xu, Shurui
    Fan, Shuanshi
    Yao, Haiyuan
    Wang, Yanhong
    Lang, Xuemei
    Lv, Pingping
    Fang, Songtian
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2017, 104 : 212 - 217
  • [5] Hydrate phase composition for multicomponent gas mixtures
    Ng, HJ
    GAS HYDRATES: CHALLENGES FOR THE FUTURE, 2000, 912 : 1034 - 1039
  • [6] A fugacity model for gas hydrate phase equilibria
    Klauda, JB
    Sandler, SI
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (09) : 3377 - 3386
  • [7] USE OF THE UNIFAC METHOD FOR CALCULATION OF PHASE-EQUILIBRIA IN MULTICOMPONENT SYSTEMS
    VIIROYA, AK
    KALLAS, YI
    SIIRDE, EK
    JOURNAL OF APPLIED CHEMISTRY OF THE USSR, 1978, 51 (11): : 2356 - 2360
  • [8] An optical microscopy method for determining stable and metastable phase equilibria involving gas hydrate and ice: Application to CO2+water systems
    Touil, Abdelhafid
    Broseta, Daniel
    FLUID PHASE EQUILIBRIA, 2025, 595
  • [9] Computation of Hydrate Phase Equilibria and Its Application to the Yamal-Europe Gas Pipeline
    Osiadacz, A.
    Uilhoorn, F. E.
    Chaczykowski, M.
    PETROLEUM SCIENCE AND TECHNOLOGY, 2009, 27 (02) : 208 - 225
  • [10] PALATNIK,LS - PHASE EQUILIBRIA IN MULTICOMPONENT SYSTEMS
    CLOKE, P
    AMERICAN MINERALOGIST, 1966, 51 (11-1) : 1821 - &