TY - JOUR
T1 - Adsorption and diffusion of H2, N2, CO, CH4 and CO2 in UTSA-16 metal-organic framework extrudates
AU - Agueda, Vicente I.
AU - Delgado, José A.
AU - Uguina, María A.
AU - Brea, Pablo
AU - Spjelkavik, Aud I.
AU - Blom, Richard
AU - Grande, Carlos
N1 - Generated from Scopus record by KAUST IRTS on 2022-09-13
PY - 2015/3/3
Y1 - 2015/3/3
N2 - Recently, a new metal-organic framework, named UTSA-16, has been proposed for removing carbon dioxide from gas mixtures by pressure swing adsorption in view of its high adsorption capacity and selectivity to this gas. Fundamental adsorption and diffusion parameters are required for designing a pressure swing adsorption (PSA) process with this adsorbent, which are lacking in the literature. In this work, adsorption Henry[U+05F3]s law constants and reciprocal diffusion time constants of hydrogen, nitrogen, carbon monoxide, methane and carbon dioxide on UTSA-16 extrudates have been measured. The pure gas adsorption isotherms of these gases at high pressures and different temperatures have also been measured.Based on the pure gas adsorption equilibrium and kinetic parameters, a PSA cycle for hydrogen purification from steam-methane reforming off-gas (containing hydrogen, carbon monoxide, methane and carbon dioxide) has been simulated. Introducing a rinse step, the process can yield hydrogen with 99.99-99.999% purity with 93-96% recovery and productivities between 2 and 2.8molkg-1h-1.
AB - Recently, a new metal-organic framework, named UTSA-16, has been proposed for removing carbon dioxide from gas mixtures by pressure swing adsorption in view of its high adsorption capacity and selectivity to this gas. Fundamental adsorption and diffusion parameters are required for designing a pressure swing adsorption (PSA) process with this adsorbent, which are lacking in the literature. In this work, adsorption Henry[U+05F3]s law constants and reciprocal diffusion time constants of hydrogen, nitrogen, carbon monoxide, methane and carbon dioxide on UTSA-16 extrudates have been measured. The pure gas adsorption isotherms of these gases at high pressures and different temperatures have also been measured.Based on the pure gas adsorption equilibrium and kinetic parameters, a PSA cycle for hydrogen purification from steam-methane reforming off-gas (containing hydrogen, carbon monoxide, methane and carbon dioxide) has been simulated. Introducing a rinse step, the process can yield hydrogen with 99.99-99.999% purity with 93-96% recovery and productivities between 2 and 2.8molkg-1h-1.
UR - https://linkinghub.elsevier.com/retrieve/pii/S0009250914004576
UR - http://www.scopus.com/inward/record.url?scp=84923882611&partnerID=8YFLogxK
U2 - 10.1016/j.ces.2014.08.039
DO - 10.1016/j.ces.2014.08.039
M3 - Article
SN - 0009-2509
VL - 124
SP - 159
EP - 169
JO - Chemical Engineering Science
JF - Chemical Engineering Science
ER -