Yueh-Yun Lin, Cheng-Che Wu, Yang-Jung Lai, Chi-Hsiang Ho, Muoi Tang*, Jung-Chin Tsai, Chie-Shaan Su and Yan-Ping Chen*,
{"title":"二氧化碳水合物与 2-甲氧基乙醚、1,1,3,3-四甲基胍、4-甲基吗啉、1-乙基-3-甲基咪唑氯化物、尿素和 1,3-环己烷双甲胺各添加剂的平衡条件的实验测量结果","authors":"Yueh-Yun Lin, Cheng-Che Wu, Yang-Jung Lai, Chi-Hsiang Ho, Muoi Tang*, Jung-Chin Tsai, Chie-Shaan Su and Yan-Ping Chen*, ","doi":"10.1021/acs.jced.4c0028010.1021/acs.jced.4c00280","DOIUrl":null,"url":null,"abstract":"<p >Due to decarbonization issues, there is growing concern about greenhouse gases, especially carbon dioxide (CO<sub>2</sub>). Gas hydrate research is a potential solution to energy needs and CO<sub>2</sub> storage tasks. Naturally occurring methane hydrates provide natural gas availability, while CO<sub>2</sub> hydrates are also receiving widespread attention for carbon capture, storage, and pipeline flow assurance. This study measured the thermodynamic equilibrium temperatures and pressures at the dissociation points for CO<sub>2</sub> hydrate mixtures containing various additives. These results provide fundamental data on the thermodynamic phase boundaries of CO<sub>2</sub> hydrate mixtures where three phases of hydrate (H), liquid water (L<sub>w</sub>), and vapor (V) coexisted. The equilibrium conditions for CO<sub>2</sub> with pure water and various additives including 2-methoxyethyl ether (0.20 and 0.30 mass fractions), 1,1,3,3-tetramethylguanidine (0.20 and 0.30 mass fractions), 4-methylmorpholine (0.10 and 0.20 mass fractions), 1-ethyl-3-methylimidazolium chloride (0.10, 0.20, and 0.30 mass fractions), urea (0.10, 0.20, and 0.30 mass fractions), and 1,3-cyclohexanebis(methylamine) (0.10 and 0.20 mass fractions) were experimentally measured in the pressure range of 1.54–3.58 MPa using the isochoric and temperature cycling method. These additives all had an inhibition effect on the formation of CO<sub>2</sub> hydrates, and the maximum average inhibition effect of each additive on the equilibrium temperature ranged from 5 to 11 K. To simulate seawater conditions, equilibrium conditions for CO<sub>2</sub> hydrate mixtures with three of these additives are also reported. The Clausius–Clapeyron equation was used to estimate possible hydrate structures. The results show that the CO<sub>2</sub> hydrate mixtures exhibited possible sI structures after adding each additive in this study.</p>","PeriodicalId":42,"journal":{"name":"Journal of Chemical & Engineering Data","volume":"69 9","pages":"3199–3209 3199–3209"},"PeriodicalIF":2.0000,"publicationDate":"2024-08-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Experimental Measurements for Equilibrium Conditions of Carbon Dioxide Hydrate Mixtures with Each Additive of 2-Methoxyethyl Ether, 1,1,3,3-Tetramethylguanidine, 4-Methylmorpholine, 1-Ethyl-3-Methylimidazolium Chloride, Urea, and 1,3-Cyclohexanebis(methylamine)\",\"authors\":\"Yueh-Yun Lin, Cheng-Che Wu, Yang-Jung Lai, Chi-Hsiang Ho, Muoi Tang*, Jung-Chin Tsai, Chie-Shaan Su and Yan-Ping Chen*, \",\"doi\":\"10.1021/acs.jced.4c0028010.1021/acs.jced.4c00280\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >Due to decarbonization issues, there is growing concern about greenhouse gases, especially carbon dioxide (CO<sub>2</sub>). Gas hydrate research is a potential solution to energy needs and CO<sub>2</sub> storage tasks. Naturally occurring methane hydrates provide natural gas availability, while CO<sub>2</sub> hydrates are also receiving widespread attention for carbon capture, storage, and pipeline flow assurance. This study measured the thermodynamic equilibrium temperatures and pressures at the dissociation points for CO<sub>2</sub> hydrate mixtures containing various additives. These results provide fundamental data on the thermodynamic phase boundaries of CO<sub>2</sub> hydrate mixtures where three phases of hydrate (H), liquid water (L<sub>w</sub>), and vapor (V) coexisted. 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引用次数: 0
摘要
由于脱碳问题,人们越来越关注温室气体,尤其是二氧化碳(CO2)。天然气水合物研究是能源需求和二氧化碳储存任务的潜在解决方案。天然存在的甲烷水合物可提供天然气,而二氧化碳水合物在碳捕获、储存和管道流量保证方面也受到广泛关注。本研究测量了含有各种添加剂的二氧化碳水合物混合物解离点的热力学平衡温度和压力。这些结果提供了二氧化碳水合物热力学相界的基本数据,其中水合物(H)、液态水(Lw)和蒸汽(V)三相共存。二氧化碳与纯水和各种添加剂(包括 2-甲氧基乙基醚(0.20 和 0.30 质量分数)、1,1,3,3-四甲基胍(0.20 和 0.30 质量分数)、4-甲基吗啉(0.10 和 0.20 质量分数)、1-乙基-3-甲基氯化咪唑(0.10、0.20 和 0.30 质量分数)、尿素(0.10、0.20 和 0.30 质量分数)和 1,3-环己烷双(甲胺)(0.10 和 0.20 质量分数)。这些添加剂都对 CO2 水合物的形成有抑制作用,每种添加剂对平衡温度的最大平均抑制作用在 5 至 11 K 之间。为了模拟海水条件,还报告了含有其中三种添加剂的 CO2 水合物混合物的平衡条件。使用克劳修斯-克拉皮隆方程估算了可能的水合物结构。结果表明,在本研究中添加每种添加剂后,二氧化碳水合物混合物都表现出可能的 sI 结构。
Experimental Measurements for Equilibrium Conditions of Carbon Dioxide Hydrate Mixtures with Each Additive of 2-Methoxyethyl Ether, 1,1,3,3-Tetramethylguanidine, 4-Methylmorpholine, 1-Ethyl-3-Methylimidazolium Chloride, Urea, and 1,3-Cyclohexanebis(methylamine)
Due to decarbonization issues, there is growing concern about greenhouse gases, especially carbon dioxide (CO2). Gas hydrate research is a potential solution to energy needs and CO2 storage tasks. Naturally occurring methane hydrates provide natural gas availability, while CO2 hydrates are also receiving widespread attention for carbon capture, storage, and pipeline flow assurance. This study measured the thermodynamic equilibrium temperatures and pressures at the dissociation points for CO2 hydrate mixtures containing various additives. These results provide fundamental data on the thermodynamic phase boundaries of CO2 hydrate mixtures where three phases of hydrate (H), liquid water (Lw), and vapor (V) coexisted. The equilibrium conditions for CO2 with pure water and various additives including 2-methoxyethyl ether (0.20 and 0.30 mass fractions), 1,1,3,3-tetramethylguanidine (0.20 and 0.30 mass fractions), 4-methylmorpholine (0.10 and 0.20 mass fractions), 1-ethyl-3-methylimidazolium chloride (0.10, 0.20, and 0.30 mass fractions), urea (0.10, 0.20, and 0.30 mass fractions), and 1,3-cyclohexanebis(methylamine) (0.10 and 0.20 mass fractions) were experimentally measured in the pressure range of 1.54–3.58 MPa using the isochoric and temperature cycling method. These additives all had an inhibition effect on the formation of CO2 hydrates, and the maximum average inhibition effect of each additive on the equilibrium temperature ranged from 5 to 11 K. To simulate seawater conditions, equilibrium conditions for CO2 hydrate mixtures with three of these additives are also reported. The Clausius–Clapeyron equation was used to estimate possible hydrate structures. The results show that the CO2 hydrate mixtures exhibited possible sI structures after adding each additive in this study.
期刊介绍:
The Journal of Chemical & Engineering Data is a monthly journal devoted to the publication of data obtained from both experiment and computation, which are viewed as complementary. It is the only American Chemical Society journal primarily concerned with articles containing data on the phase behavior and the physical, thermodynamic, and transport properties of well-defined materials, including complex mixtures of known compositions. While environmental and biological samples are of interest, their compositions must be known and reproducible. As a result, adsorption on natural product materials does not generally fit within the scope of Journal of Chemical & Engineering Data.