Supporting information to Do N-doped activated carbons truly outperform N-free activated carbons for CO2 separation in humid conditions? [Dataset]
Supporting information to Do N-doped activated carbons truly outperform N-free activated carbons for CO2 separation in humid conditions? [Dataset]
Figure S1. Comparison of pressure and fugacity values for CO2 and N2 up to 35 bars.-- Mathematical model for the simulation of breakthrough curves:Table 1, Particle and bed parameters; Table 2, Mass transfer parameters; Table 3, Energy transfer parameters; Table 4, Momentum Parameters; Table S1. Fitting parameters of the Dual-Site Langmuir adsorption model; Table S2. Comparison of literature data on CO2 uptake at different temperatures and sample N content; Table S3. Fitting parameters of the Do and Do adsorption model; Figure S2. Selectivity of CO2 over N2 at 1 bar (15 vol.% CO2/ 85 vol.% N2) at different temperatures compared to normalized N-content (divided by BET area) both in the bulk phase (wt.%, top graph) and at the surface (at.%, bottom graph).
This work was supported by the TALiSMAN and TALiSMAN2 projects funded by ERDF and the CATALPA project (ANR-22-PESP-0007) funded by the ANR France 2030 program.
Figure S1: Source: fugacity data obtained from REFPROP software database by NIST.-- Under a Creative Commons License BY-NC-ND 4.0.
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water vapour, CO2 separation, Ensure access to affordable, reliable, sustainable and modern energy for all, Adsorption, Water vapour, N-doping, http://metadata.un.org/sdg/7
water vapour, CO2 separation, Ensure access to affordable, reliable, sustainable and modern energy for all, Adsorption, Water vapour, N-doping, http://metadata.un.org/sdg/7
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