Phase Equilibrium Data for Semiclathrate Hydrate of Synthesized Binary CO2/CH4 Gas Mixture in Tetra-n-butylammonium Bromide Aqueous Solution

doi:10.1021/acs.jced.6b00876

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	Phase Equilibrium Data for Semiclathrate Hydrate of Synthesized Binary CO2/CH4 Gas Mixture in Tetra-n-butylammonium Bromide Aqueous Solution
	Zane, Xiaoya 1,2,3; Liang, Deqing1,2,3
	2017-02-01
发表期刊	JOURNAL OF CHEMICAL AND ENGINEERING DATA
卷号	62 期号:2 页码:851-856
摘要	Hydrate-based gas separation(HBGS) technology based on tetra n n-butyl ammonium bromide (TBAB) semiclathrare hydrate can be utilized in CO2 separation from biogas. The phase equilibria of semiclathrate hydrates are crucial for the successful industrial application of HBGS technology. In this work, the phase equilibrium data of TBAB semiclathrate hydrate with a 2 6 synthesized binary CO2/CH4 mixed gas (0.5 CO2 and 0.5 CH4 in mole fraction) were reported at five different TBAB concentrations (0.001, 0.01, 0.05, 0.1, and 0.2 mass fraction). The experiments were conducted in the temperature range (278.1 to 292.6) K and pressure range (2.17 to 8.16) MPa using an isochoric method. The agreement between the experimental data and the data reported in the literature indicated the reliability of the apparatus and method. The results showed that there were no obvious thermodynamic promotion effects on the CO2/CH4 mixed gas hydrate phase equilibrium conditions when the mass fraction of TBAB was less than 0.01, while there was a significant affect on the CO2/CH4 mixed gas hydrate phase equilibrium conditions when the mass fraction of TBAB was greater than 0.05. In addition, the results also indicated that the promotion effect of TBAB on the CO2/CH4 gas hydrate formation may be varied as the concentration of TBAB in the aqueous solutions changes.
文章类型	Article
WOS标题词	Science & Technology ; Physical Sciences ; Technology
DOI	10.1021/acs.jced.6b00876
研究领域[WOS]	Thermodynamics ; Chemistry ; Engineering
关键词[WOS]	CARBON-DIOXIDE CAPTURE ; AMMONIUM-CHLORIDE TBAC ; FLUE-GAS ; NATURAL-GAS ; CO2 CAPTURE ; SEPARATION PROCESS ; METHANE ; WATER ; CH4 ; THF
收录类别	SCI
语种	英语
项目资助者	NSFC(51676197) ; CAS Program(KGZD-EW-301)
WOS类目	Thermodynamics ; Chemistry, Multidisciplinary ; Engineering, Chemical
WOS记录号	WOS:000393929600029
引用统计	被引频次：20[WOS] [WOS记录] [WOS相关记录]
文献类型	期刊论文
条目标识符	http://ir.giec.ac.cn/handle/344007/14049
专题	中国科学院广州能源研究所
作者单位	1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou Ctr Gas Hydrate Res, Guangzhou 510640, Guangdong, Peoples R China 2.CAS Key Lab Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China 3.Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China
第一作者单位	中国科学院广州能源研究所
推荐引用方式 GB/T 7714	Zane, Xiaoya,Liang, Deqing. Phase Equilibrium Data for Semiclathrate Hydrate of Synthesized Binary CO2/CH4 Gas Mixture in Tetra-n-butylammonium Bromide Aqueous Solution[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA,2017,62(2):851-856.
APA	Zane, Xiaoya,&Liang, Deqing.(2017).Phase Equilibrium Data for Semiclathrate Hydrate of Synthesized Binary CO2/CH4 Gas Mixture in Tetra-n-butylammonium Bromide Aqueous Solution.JOURNAL OF CHEMICAL AND ENGINEERING DATA,62(2),851-856.
MLA	Zane, Xiaoya,et al."Phase Equilibrium Data for Semiclathrate Hydrate of Synthesized Binary CO2/CH4 Gas Mixture in Tetra-n-butylammonium Bromide Aqueous Solution".JOURNAL OF CHEMICAL AND ENGINEERING DATA 62.2(2017):851-856.