Phase Equilibria of the Synthesized Ternary CH4/CO2/N-2 Mixed-Gas Hydrates in Tetrabutylammonium Bromide Aqueous Solutions at Different Concentrations | |
Zang, Xiaoya2,3,4,5; Wang, Jing1,2,3,4; Zhou, Xuebing2,3,4,5; Wan, Lihua2,3,4,5; Liang, Deqing2,3,4,5 | |
刊名 | JOURNAL OF CHEMICAL AND ENGINEERING DATA |
2021-03-11 | |
卷号 | 66期号:3页码:1290-1295 |
ISSN号 | 0021-9568 |
DOI | 10.1021/acs.jced.0c00933 |
通讯作者 | Liang, Deqing(liangdq@ms.giec.ac.cn) |
英文摘要 | Hydrate-based gas separation (HBGS) technology can effectively separate CH4 and CO2 in multicomponent gases. To provide the necessary basic data for the HBGS technology, the hydrate phase equilibrium conditions of a ternary gas mixture (CH4/CO2/N-2 = 0.5/0.4/0.1) were determined and compared in tetrabutylammonium bromide (TBAB) aqueous solutions with different mass fractions (0.05, 0.1, 0.2, and 0.4). The results indicated that all four concentrations of TBAB aqueous solution could shift the hydrate phase equilibrium conditions of the ternary gas mixture to higher temperatures and lower pressures; this influence was enhanced with higher TBAB concentrations. When the TBAB mass fraction was 0.4, under the same phase equilibrium pressure conditions, the phase equilibrium temperature increased by a range of approximately 9-14 K compared with that of a pure water system. Meanwhile, TBAB had a greater impact on the phase equilibrium conditions of hydrates containing larger proportions of CO2 and CH4 gas and a greater impact on the phase equilibrium conditions of CO2 and CH4 gas hydrates than on N-2 hydrate. |
资助项目 | National Natural Science Foundation of China[51676197] ; National Key Research and Development Plan of China[2017YFC0307305] ; Guangzhou Science and Technology Project[201804010411] ; Guangdong Special Support Program-Local Innovation and Entrepreneurship Team Project[2019BT02L278] ; Guangdong MEPP Fund[GDME-2018D002] ; Guangdong MEPP Fund[GDOE[2019]A39] ; Guangdong MEPP Fund[GDOE[2019]A54] ; Youth Innovation Promotion Association CAS |
WOS研究方向 | Thermodynamics ; Chemistry ; Engineering |
语种 | 英语 |
出版者 | AMER CHEMICAL SOC |
WOS记录号 | WOS:000629163700009 |
资助机构 | National Natural Science Foundation of China ; National Key Research and Development Plan of China ; Guangzhou Science and Technology Project ; Guangdong Special Support Program-Local Innovation and Entrepreneurship Team Project ; Guangdong MEPP Fund ; Youth Innovation Promotion Association CAS |
内容类型 | 期刊论文 |
源URL | [http://ir.giec.ac.cn/handle/344007/32832] |
专题 | 中国科学院广州能源研究所 |
通讯作者 | Liang, Deqing |
作者单位 | 1.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 2.Chinese Acad Sci, Guangzhou Ctr Gas Hydrate Res, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China 3.CAS Key Lab Gas Hydrate, Guangzhou 510640, Peoples R China 4.Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Peoples R China 5.State Key Lab Nat Gas Hydrate, Beijing 100028, Peoples R China |
推荐引用方式 GB/T 7714 | Zang, Xiaoya,Wang, Jing,Zhou, Xuebing,et al. Phase Equilibria of the Synthesized Ternary CH4/CO2/N-2 Mixed-Gas Hydrates in Tetrabutylammonium Bromide Aqueous Solutions at Different Concentrations[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA,2021,66(3):1290-1295. |
APA | Zang, Xiaoya,Wang, Jing,Zhou, Xuebing,Wan, Lihua,&Liang, Deqing.(2021).Phase Equilibria of the Synthesized Ternary CH4/CO2/N-2 Mixed-Gas Hydrates in Tetrabutylammonium Bromide Aqueous Solutions at Different Concentrations.JOURNAL OF CHEMICAL AND ENGINEERING DATA,66(3),1290-1295. |
MLA | Zang, Xiaoya,et al."Phase Equilibria of the Synthesized Ternary CH4/CO2/N-2 Mixed-Gas Hydrates in Tetrabutylammonium Bromide Aqueous Solutions at Different Concentrations".JOURNAL OF CHEMICAL AND ENGINEERING DATA 66.3(2021):1290-1295. |
个性服务 |
查看访问统计 |
相关权益政策 |
暂无数据 |
收藏/分享 |
除非特别说明,本系统中所有内容都受版权保护,并保留所有权利。
修改评论