{"title":"Dynamic diffusion processes of miscible CO2 geological utilization with complex microscopic pore-throat structures","authors":"Xiaolong Chai, Leng Tian, Yuan Zhu, Haiyan Ding, Guangqing Zhang","doi":"10.1016/j.seppur.2025.131578","DOIUrl":null,"url":null,"abstract":"It is the key to transform the energy structure and restrain the greenhouse effect for CO<sub>2</sub> 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 CO<sub>2</sub> 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 CO<sub>2</sub> diffusion are established to describe the diffusion process with CO<sub>2</sub> utilization in tight formations. Second, a dynamic model of CO<sub>2</sub> diffusion in tight formation is developed based on the pressure-decay experiments and Fick’s law. Subsequently, the diffusion coefficient of CO<sub>2</sub> 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 CO<sub>2</sub> utilization in tight formations. The results show that the CO<sub>2</sub> 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 CO<sub>2</sub>. Meanwhile, the CO<sub>2</sub> 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 CO<sub>2</sub> 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<sup>−9</sup>m<sup>2</sup>/s to 14.5 × 10<sup>−9</sup>m<sup>2</sup>/s. The CO<sub>2</sub> concentration is primarily in the range of 1.0 mol/m<sup>3</sup> to 4.2 mol/m<sup>3</sup>, 3.2 mol/m<sup>3</sup> to 9.8 mol/m<sup>3</sup> and 11.8 mol/m<sup>3</sup> to 18.9 mol/m<sup>3</sup> with different diffusion coefficients, respectively. This paper provides physical simulation and theoretical analysis for the investigation and application of the diffusion processes of CO<sub>2</sub> utilization and storage in tight formations.","PeriodicalId":427,"journal":{"name":"Separation and Purification Technology","volume":"9 1","pages":""},"PeriodicalIF":8.1000,"publicationDate":"2025-01-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Separation and Purification Technology","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1016/j.seppur.2025.131578","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
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.
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.