2015
DOI: 10.1016/j.fuel.2015.07.020
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Regenerable magnesium-based sorbent for high-pressure and moderate-temperature CO2 capture: Physicochemical structures and capture performances

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Cited by 11 publications
(3 citation statements)
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References 38 publications
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“…The values of the fractal dimension (F) were always in the range of 2−3, which described the pore structure and surface fractal dimensions of the porous materials, and were obtained using the Frenkel−Halsey−Hill (FHH) equation with data from the N 2 gas adsorption−desorption isotherm. 42,43 The FHH model can be described as follows 44,45 V H…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The values of the fractal dimension (F) were always in the range of 2−3, which described the pore structure and surface fractal dimensions of the porous materials, and were obtained using the Frenkel−Halsey−Hill (FHH) equation with data from the N 2 gas adsorption−desorption isotherm. 42,43 The FHH model can be described as follows 44,45 V H…”
Section: Methodsmentioning
confidence: 99%
“…The crystalline structures of the samples were recorded via a X-ray diffractometer (Rigaku D/Max 2500pc) with Cu K radiation in the 2θ range of 10–90°. The values of the fractal dimension ( F ) were always in the range of 2–3, which described the pore structure and surface fractal dimensions of the porous materials, and were obtained using the Frenkel–Halsey–Hill (FHH) equation with data from the N 2 gas adsorption–desorption isotherm. , The FHH model can be described as follows , where P 0 and P are the saturation and equilibrium pressures, respectively, V is the volume of N 2 adsorbed at equilibrium pressure P ; H is the slope of the graph of ln V versus ln­(ln­( p 0 / p )), and C is constant. The lowest value of F ( F = 2) corresponds to a perfectly smooth surface and ordered pore size distribution, whereas as F increases, the surface becomes rough and the pore size distribution becomes disordered .…”
Section: Experimental Sectionmentioning
confidence: 99%
“…CO 2 capture using membranes operates on the principle of differences in the physical or chemical interaction between the CO 2 gas and the membrane for which the membrane is designed in such a way as to allow one gas to pass through faster than the other. The membrane modules can also be used as a gas absorption column or as a conventional membrane separation unit [124][125][126][127][128]. Although the membrane technology is relatively new, it requires high energy during separation, and it is widely known for its poor selectivity [129][130][131][132][133][134][135].…”
Section: Membrane Separationmentioning
confidence: 99%