2020
DOI: 10.1016/j.fuel.2020.118985
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Upgrading pipeline-quality natural gas to liquefied-quality via pressure swing adsorption using MIL-101(Cr) as adsorbent to remove CO2 and H2S from the gas

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Cited by 19 publications
(5 citation statements)
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“…Up to now, significant progress has been attained on the cyclic adsorption processes to achieve purities as high as 99.999 % for gas separation and purification in the way of biogas upgrading [58], natural gas sweeting [59], hydrogen purification [60], post-combustion studies [61], etc. [62].…”
Section: Cyclic Adsorption Processesmentioning
confidence: 99%
“…Up to now, significant progress has been attained on the cyclic adsorption processes to achieve purities as high as 99.999 % for gas separation and purification in the way of biogas upgrading [58], natural gas sweeting [59], hydrogen purification [60], post-combustion studies [61], etc. [62].…”
Section: Cyclic Adsorption Processesmentioning
confidence: 99%
“…Others have discussed these topics elsewhere. ,, Here the figures of merit we use are absolute CO 2 adsorption in mol/kg at 298 K and 2.5 bar (single-component data), absolute Xe adsorption capacity in mol/kg at 10 bar and 273 K (mixture data), and Xe/Kr selectivity at 10 bar and 273 K (mixture data). 2.5 bar is a reasonable pressure for natural gas upgrading, , so the data from Wilmer’s work is relevant.…”
Section: Resultsmentioning
confidence: 99%
“…While the reaction temperature and time for CH 3 COOH-MIL-101(Cr) can be reduced to 180 °C and 4 h, [106] nine of the ten entries with S BET above 3200 m 2 g −1 were still synthesized at 200-220 °C for 8 h or more. [16,21,97,[107][108][109][110][111][112] This observation may imply that lowering reaction temperatures and durations may also compromise MIL-101(Cr)'s porosity when using monocarboxylic acids as additives. However, the extent of mineralization achieved via monocarboxylic acids versus HF is unclear.…”
Section: Organic Acidsmentioning
confidence: 99%