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Biogas Cleaning via Vacuum Swing Adsorption Using a Calcium Metal-Organic Framework Adsorbent: A Multiscale Simulation Study
被引:0
作者:
Lasich, Madison
[1
]
Adeleke, Victoria T.
[1
]
Tumba, Kaniki
[1
,2
]
机构:
[1] Mangosuthu Univ Technol, Dept Chem Engn, Thermodynam Mat Separat Res Grp, ZA-4031 Umlazi, South Africa
[2] Univ Officielle Bukavu, Sch Mines, Karhale Campus,POB 570, Bukavu, DEM REP CONGO
基金:
新加坡国家研究基金会;
关键词:
vacuum swing adsorption;
multiscale modelling;
biogas;
metal-organic frameworks;
steam reforming;
CARBON-DIOXIDE;
CU-BTC;
COORDINATION POLYMER;
HYDROGEN-STORAGE;
CO2;
ADSORPTION;
SITES;
SEPARATION;
PERFORMANCE;
H-2;
DYNAMICS;
D O I:
10.3390/chemengineering8030062
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Purifying biogas can enhance the performance of distributed smart grid systems while potentially yielding clean feedstock for downstream usage such as steam reforming. Recently, a novel anion-pillared metal-organic framework (MOF) was reported in the literature that shows good capacity to separate acetylene from carbon dioxide. The present study assesses the usefulness of this adsorbent for separating a typical biogas mixture (consisting of methane, nitrogen, oxygen, hydrogen, carbon dioxide, and hydrogen sulphide) using a multiscale approach. This approach couples atomistic Monte Carlo simulations in the grand canonical ensemble with the batch equilibrium modelling of a pressure swing adsorption system. The metal-organic framework displays selectivity at low pressures for carbon dioxide and especially hydrogen sulphide. An analysis of adsorption isotherm models coupled with statistical distributions of surface-gas interaction energies determined that both CH4 and CO2 exhibited Langmuir-type adsorption, while H2S displayed Langmuir-type behaviour at low pressures, with increasing adsorption site heterogeneity at high pressures. Batch equilibrium modelling of a vacuum swing adsorption system to purify a CH4/CO2 feedstock demonstrated that such a system can be incorporated into a solar biogas reforming process since the target purity of 93-94 mol-% methane for incorporation into the process was readily achievable.
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页数:24
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