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Separation of CO2/CH4 mixtures with the MIL-53(Al) metal-organic framework
被引:311
|作者:
Finsy, V.
[1
]
Ma, L.
[1
]
Alaerts, L.
[2
]
De Vos, D. E.
[2
]
Baron, G. V.
[1
]
Denayer, J. F. M.
[1
]
机构:
[1] Vrije Univ Brussel, Dept Chem Engn Chem Ingenieurstech & Ind Scheikun, Brussels, Belgium
[2] Katholieke Univ Leuven, Ctr Oppervlaktechem Katalyse, Leuven, Belgium
关键词:
Metal-organic framework;
CO2;
CH4;
Separation;
Adsorption;
MIL-53(Al);
Polyvinyl alcohol binder;
HIGH H-2 ADSORPTION;
CARBON-DIOXIDE;
SAPO-34;
MEMBRANES;
HYDROGEN STORAGE;
XYLENE ISOMERS;
HIGH-CAPACITY;
CO2;
CAPTURE;
PORE-SIZE;
METHANE;
N-2;
D O I:
10.1016/j.micromeso.2008.11.007
中图分类号:
O69 [应用化学];
学科分类号:
081704 ;
摘要:
Adsorptive separation of CH4/CO2 mixtures was studied using a fixed-bed packed with MIL-53(Al) MOF pellets. Such pellets of MIL-53(Al) were produced using a polyvinyl alcohol binder. As revealed by N-2 adsorption isotherms, the use of polyvinyl alcohol as binder results in a loss in overall capacity of 32%. Separations of binary mixtures in breakthrough experiments were successfully performed at pressures varying between I and 8 bar and different mixture compositions. The binary adsorption isotherms reveal a preferential adsorption Of CO2 compared to CH4 over the whole pressure and concentration range. The separation selectivity was affected by total pressure: below 5 bar. a constant selectivity, with an average separation factor of about 7 was observed. Above 5 bar, the average separation factor decreases to about 4. The adsorption selectivity is affected by breathing of the framework and specific interaction Of CO2 with framework hydroxyl groups. CO2 desorption can be realised by mild thermal treatment. (C) 2008 Elsevier Inc. All rights reserved.
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页码:221 / 227
页数:7
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