{"title":"通过循环注入 N2-CO2 气体和浸泡法提高甲烷水合物的甲烷产量:缓慢扩散控制过程的意义","authors":"Masahiro Yasue , Yoshihiro Masuda, Yunfeng Liang","doi":"10.1016/j.apenergy.2024.124912","DOIUrl":null,"url":null,"abstract":"<div><div>Methane hydrate (MH) is a crucial lower-carbon energy resource in climate mitigation and current energy transition. A depressurization technique has been mainly attempted to produce methane gas. Simultaneously, the exchange of CH<sub>4</sub> from gas hydrates by N<sub>2</sub>–CO<sub>2</sub> has been studied to enhance methane gas production and CO<sub>2</sub> sequestration. We conducted experiments with hydrate-bearing cores by applying the cyclic injection and soaking method. An N<sub>2</sub>–CO<sub>2</sub> gas (ca. 60 mol% CO<sub>2</sub>) was injected into a core during the injection period, and the core was allowed to stand stationary during the soaking period. Concurrently, a numerical model was developed to simulate the gas production performance of the cyclic injection and soaking method. This model considers a two-stage process for the gas replacement phenomena between CH<sub>4</sub> and (N<sub>2</sub> + CO<sub>2</sub>) in the hydrate: an almost immediate replacement at the hydrate surface followed by a more gradual diffusion-controlled replacement in the subsurface hydrate layer. The rapid replacement is modeled by phase equilibrium between the vapor phase and the hydrate surface. The diffusion due to the difference in concentration of each gas component between the surface hydrate layer and the inner hydrate describes the slow gas replacement phenomenon. By repeating four cycles of soaking and injection, the experiments achieved a high CH<sub>4</sub> recovery factor of 67.7 % and a high exchange ratio of 54.7 %. About 18 % of the CO<sub>2</sub> injected gas was sequestrated. The soaking process enhanced methane recovery by 1.5 times in the recovery factor compared to the first injection production and almost half of the CH<sub>4</sub> molecules in MH were extracted. Our simulations demonstrated excellent agreement with experimental results, confirming the soaking process is very efficient for methane recovery. From the production history matching, the diffusion coefficient of CH<sub>4</sub> molecules in the solid-state MH during slow replacement phenomena was estimated to be on the order of 10<sup>−19</sup> m<sup>2</sup>/s, significantly smaller than those of previous research.</div></div>","PeriodicalId":246,"journal":{"name":"Applied Energy","volume":"379 ","pages":"Article 124912"},"PeriodicalIF":10.1000,"publicationDate":"2024-11-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Enhancing the methane production from methane hydrate by cyclic N2–CO2 gas injection and soaking method: Significance of the slow diffusion-controlled process\",\"authors\":\"Masahiro Yasue , Yoshihiro Masuda, Yunfeng Liang\",\"doi\":\"10.1016/j.apenergy.2024.124912\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Methane hydrate (MH) is a crucial lower-carbon energy resource in climate mitigation and current energy transition. A depressurization technique has been mainly attempted to produce methane gas. Simultaneously, the exchange of CH<sub>4</sub> from gas hydrates by N<sub>2</sub>–CO<sub>2</sub> has been studied to enhance methane gas production and CO<sub>2</sub> sequestration. We conducted experiments with hydrate-bearing cores by applying the cyclic injection and soaking method. An N<sub>2</sub>–CO<sub>2</sub> gas (ca. 60 mol% CO<sub>2</sub>) was injected into a core during the injection period, and the core was allowed to stand stationary during the soaking period. Concurrently, a numerical model was developed to simulate the gas production performance of the cyclic injection and soaking method. This model considers a two-stage process for the gas replacement phenomena between CH<sub>4</sub> and (N<sub>2</sub> + CO<sub>2</sub>) in the hydrate: an almost immediate replacement at the hydrate surface followed by a more gradual diffusion-controlled replacement in the subsurface hydrate layer. The rapid replacement is modeled by phase equilibrium between the vapor phase and the hydrate surface. The diffusion due to the difference in concentration of each gas component between the surface hydrate layer and the inner hydrate describes the slow gas replacement phenomenon. By repeating four cycles of soaking and injection, the experiments achieved a high CH<sub>4</sub> recovery factor of 67.7 % and a high exchange ratio of 54.7 %. About 18 % of the CO<sub>2</sub> injected gas was sequestrated. The soaking process enhanced methane recovery by 1.5 times in the recovery factor compared to the first injection production and almost half of the CH<sub>4</sub> molecules in MH were extracted. Our simulations demonstrated excellent agreement with experimental results, confirming the soaking process is very efficient for methane recovery. From the production history matching, the diffusion coefficient of CH<sub>4</sub> molecules in the solid-state MH during slow replacement phenomena was estimated to be on the order of 10<sup>−19</sup> m<sup>2</sup>/s, significantly smaller than those of previous research.</div></div>\",\"PeriodicalId\":246,\"journal\":{\"name\":\"Applied Energy\",\"volume\":\"379 \",\"pages\":\"Article 124912\"},\"PeriodicalIF\":10.1000,\"publicationDate\":\"2024-11-26\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Applied Energy\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0306261924022955\",\"RegionNum\":1,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Applied Energy","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0306261924022955","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
Enhancing the methane production from methane hydrate by cyclic N2–CO2 gas injection and soaking method: Significance of the slow diffusion-controlled process
Methane hydrate (MH) is a crucial lower-carbon energy resource in climate mitigation and current energy transition. A depressurization technique has been mainly attempted to produce methane gas. Simultaneously, the exchange of CH4 from gas hydrates by N2–CO2 has been studied to enhance methane gas production and CO2 sequestration. We conducted experiments with hydrate-bearing cores by applying the cyclic injection and soaking method. An N2–CO2 gas (ca. 60 mol% CO2) was injected into a core during the injection period, and the core was allowed to stand stationary during the soaking period. Concurrently, a numerical model was developed to simulate the gas production performance of the cyclic injection and soaking method. This model considers a two-stage process for the gas replacement phenomena between CH4 and (N2 + CO2) in the hydrate: an almost immediate replacement at the hydrate surface followed by a more gradual diffusion-controlled replacement in the subsurface hydrate layer. The rapid replacement is modeled by phase equilibrium between the vapor phase and the hydrate surface. The diffusion due to the difference in concentration of each gas component between the surface hydrate layer and the inner hydrate describes the slow gas replacement phenomenon. By repeating four cycles of soaking and injection, the experiments achieved a high CH4 recovery factor of 67.7 % and a high exchange ratio of 54.7 %. About 18 % of the CO2 injected gas was sequestrated. The soaking process enhanced methane recovery by 1.5 times in the recovery factor compared to the first injection production and almost half of the CH4 molecules in MH were extracted. Our simulations demonstrated excellent agreement with experimental results, confirming the soaking process is very efficient for methane recovery. From the production history matching, the diffusion coefficient of CH4 molecules in the solid-state MH during slow replacement phenomena was estimated to be on the order of 10−19 m2/s, significantly smaller than those of previous research.
期刊介绍:
Applied Energy serves as a platform for sharing innovations, research, development, and demonstrations in energy conversion, conservation, and sustainable energy systems. The journal covers topics such as optimal energy resource use, environmental pollutant mitigation, and energy process analysis. It welcomes original papers, review articles, technical notes, and letters to the editor. Authors are encouraged to submit manuscripts that bridge the gap between research, development, and implementation. The journal addresses a wide spectrum of topics, including fossil and renewable energy technologies, energy economics, and environmental impacts. Applied Energy also explores modeling and forecasting, conservation strategies, and the social and economic implications of energy policies, including climate change mitigation. It is complemented by the open-access journal Advances in Applied Energy.