Kinetic Modeling of Hydrogen Generation via In Situ Combustion Gasification of Heavy Oil

被引:0
|
作者
Ifticene, Mohamed Amine [1 ]
Li, Yunan [2 ]
Song, Ping [1 ]
Yuan, Qingwang [1 ]
机构
[1] Texas Tech Univ, Bob L Herd Dept Petr Engn, Lubbock, TX 79409 USA
[2] Stanford Univ, Energy Sci & Engn, Stanford, CA 94305 USA
关键词
LOW-TEMPERATURE OXIDATION; SIMULATION; FRONT;
D O I
10.1021/acs.energyfuels.4c03237
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the global push for sustainable energy, in situ combustion gasification (ISCG) has emerged as a transformative technology to leverage the world's abundant heavy oil reserves for producing carbon-zero hydrogen. Chemical kinetics are crucial for modeling subsurface hydrogen generation and optimizing production schemes to maximize hydrogen yield, which are however currently lacking. This study aims to develop the first experimentally validated kinetic model for hydrogen generation during ISCG of heavy oil. To accurately model ISCG reactions, particularly hydrogen generation, we combined kinetic cell experiments with numerical modeling to history match the experimental results. The temporal variation of generated gases, such as hydrogen, measured in laboratory experiments, served as the baseline for history matching. A differential evolution optimization algorithm was employed to calibrate the kinetic parameters of the numerical model with experimental results. The kinetic model for combustion reactions was accurately calibrated after 454 optimization runs with a history-matching error of 3.46%. This accuracy is attributed to the well-studied nature of heavy oil oxidation and the comprehensive reaction scheme employed. Conversely, calibrating the kinetic model for gasification reactions with kinetic cell experimental results proved more challenging yielding a history-matching error of 22.19% after 488 optimization runs. Despite significant uncertainties in hydrogen generation and consumption reactions due to limited knowledge of the gasification process, our proposed kinetic model can still predict hydrogen generation with a simplified but powerful reaction scheme, compared to previously proposed ISCG models that involve numerous reactions. This work introduces the first kinetic model to describe the hydrogen generation process during ISCG of heavy oil with rigorous experimental validation. This reliable kinetic model establishes a solid foundation for future multiscale reservoir simulation and further optimization of the field development for enhanced hydrogen production in a more sustainable manner.
引用
收藏
页码:19787 / 19797
页数:11
相关论文
共 50 条
  • [31] An experimental investigation on hydrogen generation from in-situ gasification by pyrolysis
    Tang, Xiaodong
    Pu, Wanfen
    Chen, Qingyuan
    Liu, Renbao
    Yang, Yu
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2024, 49 : 1019 - 1027
  • [32] Modelling hydrogen production by the rich combustion of heavy fuel oil
    Gomez, J.
    Mmbaga, J. P.
    Hayes, R. E.
    Toledo, M.
    Gracia, F.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (40) : 17933 - 17943
  • [33] Properties, combustion behavior, and kinetic triplets of coke produced by low-temperature oxidation and pyrolysis: Implications for heavy oil in-situ combustion
    Zhao, Shuai
    Pu, Wan-Fen
    Su, Lei
    Shang, Ce
    Song, Yang
    Li, Wei
    He, Hui-Zhuo
    Liu, Yi-Gang
    Liu, Zhe-Zhi
    PETROLEUM SCIENCE, 2021, 18 (05) : 1483 - 1491
  • [34] Properties, combustion behavior, and kinetic triplets of coke produced by low-temperature oxidation and pyrolysis: Implications for heavy oil in-situ combustion
    Shuai Zhao
    Wan-Fen Pu
    Lei Su
    Ce Shang
    Yang Song
    Wei Li
    Hui-Zhuo He
    Yi-Gang Liu
    Zhe-Zhi Liu
    Petroleum Science, 2021, 18 (05) : 1483 - 1491
  • [35] In situ upgrading of Llancanelo heavy oil using in situ combustion and a downhole catalyst bed
    Cavallaro, A. N.
    Galliano, G. R.
    Moore, R. G.
    Mehta, S. A.
    Ursenbach, M. G.
    Zalewski, E.
    Pereira, P.
    JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 2008, 47 (09): : 23 - 31
  • [36] Applicability of Kinetic Models for In Situ Combustion Processes with Different Oil Types
    Na Jia
    David H.-S. Law
    Paul Naccache
    Marie Ann Giddins
    Natural Resources Research, 2017, 26 : 37 - 55
  • [37] Kinetic Modelling of the In-Situ Combustion Process for Athabasca Oil Sands
    Chen, Xiaolin
    Chen, Zhangxin
    Moore, Robert Gordon
    Mehta, Sudarshan A.
    Ursenbach, Matthew G.
    Harding, Thomas Grant
    JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 2015, 54 (01): : 12 - 14
  • [38] Predictability of Crude Oil In-Situ Combustion by the Isoconversional Kinetic Approach
    Cinar, Murat
    Hascakir, Berna
    Castanier, Louis M.
    Kovscek, Anthony R.
    SPE JOURNAL, 2011, 16 (03): : 537 - 547
  • [39] Applicability of Kinetic Models for In Situ Combustion Processes with Different Oil Types
    Jia, Na
    Law, David H. -S.
    Naccache, Paul
    Giddins, Marie Ann
    NATURAL RESOURCES RESEARCH, 2017, 26 (01) : 37 - 55
  • [40] Potential for hydrogen generation from in situ combustion of Athabasca bitumen
    Kapadia, Punitkumar R.
    Kallos, Michael S.
    Gates, Ian D.
    FUEL, 2011, 90 (06) : 2254 - 2265