Methane recovery from natural gas hydrate in porous sediment using pressurized liquid CO2

被引:154
|
作者
Yuan, Qing [1 ,2 ]
Sun, Chang-Yu [1 ]
Liu, Bei [1 ]
Wang, Xue [1 ]
Ma, Zheng-Wei [1 ]
Ma, Qing-Lan [1 ]
Yang, Lan-Ying [1 ]
Chen, Guang-Jin [1 ]
Li, Qing-Ping [3 ]
Li, Shi [2 ]
Zhang, Ke [2 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] PetroChina, Res Inst Petr Explorat & Dev, Beijing 100083, Peoples R China
[3] CNOOC Res Ctr, Beijing 100027, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrate; Methane; Liquid CO2; CO2-CH4; replacement; CARBON-DIOXIDE SEQUESTRATION; MOLECULAR-DYNAMICS; REPLACEMENT; DISSOCIATION; CH4; EXPLOITATION; SIMULATION;
D O I
10.1016/j.enconman.2012.11.018
中图分类号
O414.1 [热力学];
学科分类号
摘要
The dynamics of CH4 replacement in natural gas hydrate with liquid CO2 was studied with a high pressure three-dimensional reactor. Five groups of hydrate samples were formed to investigate the effect of hydrate reservoir properties on CH4-CO2 replacement reaction. The results showed that CH4 in the hydrate gradually moves to the liquid CO2 phase while CO2 in the liquid phase penetrates into the hydrate under pressure-temperature conditions not only within the phase zone surrounded by (L-CO2-V-CO2), (water-H-CO2-L-CO2), and (water-H-CH4-V-CH4) curves but also that above (L-CO2-V-CO2) and (water-H-CH4-V-CH4) curves. The replacement rate and amount of CH4 increase with the increase of hydrate saturation in the sediments. Compared with injecting gaseous CO2 method, liquid CO2 injection is also benefit for the recovery of CH4 from hydrate reservoir with much free water or that without underlying gas room to the extent that the injection of liquid CO2 is kept by high gas saturation. The replacement percent of CH4 hydrate decreases with the increase of hydrate saturation, but increases with the increase of water saturation. A higher replacement percent is obtained in the zone surrounded by three phase curves of (L-CO2-V-CO2), (water-H-CO2-L-CO2) and (water-H-CH4-V-CH4). (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:257 / 264
页数:8
相关论文
共 50 条
  • [41] Regimes of methane recovery from gas hydrate on injection of "warm" carbon dioxide into a porous medium
    Shagapov, V. Sh.
    Khasanov, M. K.
    HIGH TEMPERATURE, 2017, 55 (05) : 737 - 745
  • [42] Integration of CO2 cryogenic removal with a natural gas pressurized liquefaction process using gas expansion refrigeration
    Xiong, Xiaojun
    Lin, Wensheng
    Gu, Anzhong
    ENERGY, 2015, 93 : 1 - 9
  • [43] Advances in research on CO2 replacement for natural gas hydrate exploitation
    Bai M.
    Zhang Z.
    Chen Q.
    Xu L.
    Du S.
    Liu Y.
    Oil and Gas Geology, 2024, 45 (02): : 553 - 564
  • [44] Advance on simulation exploitation of natural gas hydrate by replacement with CO2
    Li, X. (lixs@ms.giec.ac.cn), 1600, Materials China (64):
  • [45] Mesoscale Modeling of Exploiting Methane Hydrate by CO2 Replacement in Homogeneous Porous Media
    Hsieh, Pei-Ying
    Sean, Wu-Yang
    Sato, Toru
    Seo, Yong-Won
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2020, 158
  • [46] Feasibility of simultaneous CO2 storage and CH4 production from natural gas hydrate using mixtures of CO2 and N2
    Kvamme, Bjorn
    CANADIAN JOURNAL OF CHEMISTRY, 2015, 93 (08) : 897 - 905
  • [47] Modeling of methane gas recovery from geo-pressured saline aquifers using CO2 sequestration
    Warnecki, Marcin
    NAFTA-GAZ, 2016, 72 (06): : 393 - 402
  • [48] Continuous seperation of CO2 from a H2 + CO2 gas mixture using clathrate hydrate
    Horii, Shunsuke
    Ohmura, Ryo
    APPLIED ENERGY, 2018, 225 : 78 - 84
  • [49] Effects of salinity on hydrate stability and implications for storage of CO2 in natural gas hydrate reservoirs
    Husebo, Jarle
    Ersland, Geir
    Graue, Arne
    Kvamme, Bjorn
    GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01): : 3731 - 3738
  • [50] Transport phenomena of liquid CO2 in pressurized water flow with clathrate-hydrate at the interface
    Hirai, S
    Okazaki, K
    Araki, N
    Yazawa, H
    Ito, H
    Hijikata, K
    ENERGY CONVERSION AND MANAGEMENT, 1996, 37 (6-8) : 1073 - 1078