Dynamic diffusion processes of miscible CO2 geological utilization with complex microscopic pore-throat structures

IF 9 1区 工程技术 Q1 ENGINEERING, CHEMICAL Separation and Purification Technology Pub Date : 2025-07-30 Epub Date: 2025-01-13 DOI:10.1016/j.seppur.2025.131578
Xiaolong Chai , Leng Tian , Yuan Zhu , Haiyan Ding , Guangqing Zhang
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Abstract

It is the key to transform the energy structure and restrain the greenhouse effect for CO2 utilization and storage. Tight reservoir has attracted special attentions due to the huge reserves and mature technology. The gas diffusion is a main and important element to improve the CO2 utilization efficiency and storage potential. In this paper, first, the pore constructure, pore pressure and confining pressure are simulated and a series of experiments of CO2 diffusion are established to describe the diffusion process with CO2 utilization in tight formations. Second, a dynamic model of CO2 diffusion in tight formation is developed based on the pressure-decay experiments and Fick’s law. Subsequently, the diffusion coefficient of CO2 is ensured by fitting experimental results, and the accuracy of established model is also evaluated. Finally, the effects of water slug, permeability, temperature and diffusion coefficient on diffusion rate, concentration distribution, diffusion front and diffusion distance at different stage are investigated, and the diffusion distance under different temperature, diffusion coefficients and diffusion time are charactered quantitatively in the processes of CO2 utilization in tight formations. The results show that the CO2 diffusion rate at stage I and II is 0.075 cm/d–0.15 cm/d and 0.18 cm/d–1.62 cm/d respectively, and the water slug will weaken the diffusion rate of CO2. Meanwhile, the CO2 concentration in the upper part of the core is high due to the effect of gravity overlap, which will reduce the oil’s flow capacity and sweep efficiency. The diffusion rate, concentration and diffusion distance will increase when the temperature rises form 58 ℃ to 88 ℃, and the effects of temperature on diffusion characteristics at stage I of CO2 diffusion are weaker than that of stage II. The diffusion time of reaching the boundary is 90000 s, 60000 s and 30000 s at stage I, and is 190000 s 160000 s and 130000 s at stage II, respectively when the diffusion coefficients rise from 1.45 × 10−9m2/s to 14.5 × 10−9m2/s. The CO2 concentration is primarily in the range of 1.0 mol/m3 to 4.2 mol/m3, 3.2 mol/m3 to 9.8 mol/m3 and 11.8 mol/m3 to 18.9 mol/m3 with different diffusion coefficients, respectively. This paper provides physical simulation and theoretical analysis for the investigation and application of the diffusion processes of CO2 utilization and storage in tight formations.
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复杂微观孔喉结构下混相CO2地质利用的动态扩散过程
二氧化碳的利用与封存是转变能源结构、抑制温室效应的关键。致密储层以其巨大的储量和成熟的技术引起了人们的特别关注。气体扩散是提高CO2利用效率和储存潜力的重要因素。本文首先对致密储层孔隙结构、孔隙压力和围压进行了模拟,建立了一系列CO2扩散实验,描述了致密储层利用CO2的扩散过程。其次,基于压力衰减实验和菲克定律建立了致密地层中CO2扩散的动态模型。通过拟合实验结果,确定了CO2的扩散系数,并对所建立模型的精度进行了评价。最后,研究了水段塞、渗透率、温度和扩散系数对不同阶段的扩散速率、浓度分布、扩散锋和扩散距离的影响,定量表征了致密储层CO2利用过程中不同温度、扩散系数和扩散时间下的扩散距离。结果表明:第一阶段和第二阶段CO2的扩散速率分别为0.075 cm/d - 0.15 cm/d和0.18 cm/d - 1.62 cm/d,水段塞会减弱CO2的扩散速率;同时,由于重力重叠的影响,岩心上部CO2浓度较高,会降低原油的流动能力和波及效率。当温度从58℃升高到88℃时,扩散速率、浓度和扩散距离均增大,且温度对CO2扩散第一阶段扩散特性的影响弱于第二阶段。扩散系数从1.45 × 10−9m2/s上升到14.5 × 10−9m2/s时,扩散到达边界的时间在阶段I分别为90000 s、60000 s和30000 s,阶段II分别为19000 s、160000 s和130000 s。不同扩散系数下CO2浓度主要分布在1.0 mol/m3 ~ 4.2 mol/m3、3.2 mol/m3 ~ 9.8 mol/m3和11.8 mol/m3 ~ 18.9 mol/m3范围内。本文为致密地层中CO2利用和封存扩散过程的研究和应用提供了物理模拟和理论分析。
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来源期刊
Separation and Purification Technology
Separation and Purification Technology 工程技术-工程:化工
CiteScore
14.00
自引率
12.80%
发文量
2347
审稿时长
43 days
期刊介绍: Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.
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