Study on three-phase flow characteristics of natural gas hydrate pipeline transmission

被引:28
作者
Chen, Wei [1 ,2 ]
Xu, Hai-Liang [1 ]
Kong, Wei-Yang [1 ]
Yang, Fang-qiong [1 ]
机构
[1] Cent South Univ, Sch Mech & Elect Engn, Changsha 410083, Hunan, Peoples R China
[2] Hunan Univ Humanities Sci & Technol, Dept Energy & Elect Engn, Loudi 417000, Hunan, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas hydrate; Pipeline transmission; Solid-liquid-gas three-phase flow; Numerical simulation; Pressure loss gradient; TEMPERATURE; SIMULATION; DECOMPOSITION;
D O I
10.1016/j.oceaneng.2020.107727
中图分类号
U6 [水路运输]; P75 [海洋工程];
学科分类号
0814 ; 081505 ; 0824 ; 082401 ;
摘要
Based on the basic principles of thermodynamics and fluid mechanics, the temperature and pressure model of natural gas hydrate hydraulic lifting pipeline, the hydrate decomposition mass transfer model and the mathematical model of pipeline multiphase flow are established. The relationship between the back pressure of the pipeline outlet, the decomposition surface and the depth of the seawater was analyzed. On this basis, the numerical simulation and experimental verification of natural gas hydrate pipeline transmission were carried out. The effects of pipe diameter, inlet velocity and solid phase parameters on the three-phase flow of natural gas hydrate pipelines were analyzed. The result shows that with the outlet pressure increasing, the position at which the hydrate begins to decompose moves up and the decomposition rate slows down. As the depth of mining increases, the rate of hydrate decomposition slows and the position at which decomposition begins to move up. In deep sea mining below 1500 m, the increase of mining depth has little effect on the decomposition rate of hydrate, and the decomposition starting position is always near 510 m in sea depth. The pipe pressure loss gradient decreases as the pipe diameter increases. After the pipe diameter is larger than 300 mm, the pressure loss gradient decreases slowly, and the pressure loss gradient drops sharply at 450 mm, and eventually stabilizes after 500 mm. When the inlet velocity of the pipe is low, the fluid flow in the pipe is unstable and reflow occurs. The pipe pressure loss gradient first decreases and then increases as the fluid flow rate increases, and there is an optimal flow rate value that minimizes the pressure loss gradient.
引用
收藏
页数:17
相关论文
共 39 条
  • [1] Surface wave effects on water temperature in the Baltic Sea: simulations with the coupled NEMO-WAM model
    Alari, Victor
    Staneva, Joanna
    Breivik, Oyvind
    Bidlot, Jean-Raymond
    Mogensen, Kristian
    Janssen, Peter
    [J]. OCEAN DYNAMICS, 2016, 66 (08) : 917 - 930
  • [2] Variations in submarine groundwater runoff as a possible cause of decomposition of marine methane-hydrates in the Artcic
    Dzyuba, A. V.
    Zektser, I. S.
    [J]. WATER RESOURCES, 2013, 40 (01) : 74 - 83
  • [3] NON-LINEAR STATIC ANALYSIS OF DEEP OCEAN MINING PIPE .1. MODELING AND FORMULATION
    FELIPPA, CA
    CHUNG, JS
    [J]. JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 1981, 103 (01): : 11 - 15
  • [4] [付建红 Fu Jianhong], 2015, [石油学报, Acta Petrolei Sinica], V36, P232
  • [5] Goyal M.K., 2010, CHIN J THEOR APPL ME, V41, P155
  • [6] Gas hydrate decomposition rate in flowing water
    Hamaguchi, Ryokichi
    Nishimura, Yuki
    Inoue, Gen
    Matsukuma, Yosuke
    Minemoto, Masaki
    [J]. JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2007, 129 (02): : 102 - 106
  • [7] Modeling of Conjugated Heat Transfer in Direct-Contact Membrane Distillation of Seawater Desalination Systems
    Ho, Chii-Dong
    Yang, Tzu-Jing
    Wang, Bo-Cheng
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2012, 35 (10) : 1765 - 1776
  • [8] Experimental and analytical investigations of airlift pumps operating in three-phase flow
    Kassab, S. Z.
    Kandil, H. A.
    Warda, H. A.
    Ahmed, W. H.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2007, 131 (1-3) : 273 - 281
  • [9] Kato H., 2008, JSME INT J, V18, P286
  • [10] KINETICS OF METHANE HYDRATE DECOMPOSITION
    KIM, HC
    BISHNOI, PR
    HEIDEMANN, RA
    RIZVI, SSH
    [J]. CHEMICAL ENGINEERING SCIENCE, 1987, 42 (07) : 1645 - 1653