沼气
甲烷
笼状水合物
气体分离
水合物
化学
分离过程
水溶液
化学工程
材料科学
分析化学(期刊)
色谱法
废物管理
膜
有机化学
物理化学
工程类
生物化学
作者
Qian Xue,Faping Liu,Zunzhao Li,Xiaolin Wang,Xu Andy Sun,Mingrui Liu,Peixian Wang,Shuanshi Fan,Xuemei Lang
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2023-07-18
卷期号:37 (15): 11142-11151
标识
DOI:10.1021/acs.energyfuels.3c01119
摘要
Hydrate-based separation and capture technology, as a green and economical gas separation technology, can be used to purify biogas by removing CO2 to increase the calorific value and energy density. To achieve pilot-scale biogas separation, a 15 L pilot-scale reactor with novel jet impingement stream was designed for fast and efficient CH4 recovery and CO2 capture and pure CH4 was obtained by multistage separation in this work. Hydrate nucleation and growth were enhanced by jet impingement stream in aqueous solution with 5.0 wt % tetrabutylammonium bromide. The space velocity of the reactor reached a maximum value of 557 h–1; the gas uptake reached up to 1.00 mol/L at 4.0 MPa; and the fastest time to reach 80% of the rate of gas uptake was about 2.5 min at 3.0 MPa and 277 K. The effects of the pressure and temperature driving force on the CH4 concentration in residual gas, CH4 recovery rate, CO2 capture ratio, and gas hydration rate were studied. By a four-stage hydrate-based gas separation process, the CH4 concentration could be increased from 50.0 to about 95.1%. This work provides insights for the industrial application of continuous hydrate-based biogas separation.
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