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

IF 5.2 3区 工程技术 Q2 ENERGY & FUELS Energy & Fuels Pub Date : 2024-10-08 DOI:10.1021/acs.energyfuels.4c0323710.1021/acs.energyfuels.4c03237
Mohamed Amine Ifticene, Yunan Li, Ping Song and Qingwang Yuan*, 
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Abstract

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.

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重油原位燃烧气化制氢的动力学建模
在全球推动可持续能源发展的过程中,原地燃烧气化(ISCG)已成为一项变革性技术,可利用全球丰富的重油储量生产零碳氢气。化学动力学对于建立地下氢气生成模型和优化生产方案以最大限度地提高氢气产量至关重要,但目前还缺乏这方面的研究。本研究旨在为重油 ISCG 过程中的氢气生成建立首个经过实验验证的动力学模型。为了准确模拟 ISCG 反应,特别是氢气生成,我们将动力学电池实验与数值建模相结合,使其与实验结果相吻合。实验室实验中测得的氢气等生成气体的时间变化是历史匹配的基准。采用差分进化优化算法将数值模型的动力学参数与实验结果进行校准。经过 454 次优化运行后,燃烧反应动力学模型得到了精确校准,历史匹配误差为 3.46%。这一准确性归功于对重油氧化的深入研究和所采用的全面反应方案。相反,用动力学电池实验结果校准气化反应动力学模型则更具挑战性,经过 488 次优化运行后,历史匹配误差达到 22.19%。尽管由于对气化过程的了解有限,氢气生成和消耗反应存在很大的不确定性,但与之前提出的涉及众多反应的 ISCG 模型相比,我们提出的动力学模型仍能通过简化但功能强大的反应方案预测氢气生成。这项研究首次提出了描述重油 ISCG 制氢过程的动力学模型,并经过了严格的实验验证。这一可靠的动力学模型为未来的多尺度油藏模拟和进一步优化油田开发奠定了坚实的基础,从而以更可持续的方式提高氢气产量。
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来源期刊
Energy & Fuels
Energy & Fuels 工程技术-工程:化工
CiteScore
9.20
自引率
13.20%
发文量
1101
审稿时长
2.1 months
期刊介绍: Energy & Fuels publishes reports of research in the technical area defined by the intersection of the disciplines of chemistry and chemical engineering and the application domain of non-nuclear energy and fuels. This includes research directed at the formation of, exploration for, and production of fossil fuels and biomass; the properties and structure or molecular composition of both raw fuels and refined products; the chemistry involved in the processing and utilization of fuels; fuel cells and their applications; and the analytical and instrumental techniques used in investigations of the foregoing areas.
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