Tuning the Gas Separation Performance of CuBTC by Ionic Liquid Incorporation.

DOI: 10.1021/acs.langmuir.5b04123

Jan. 1, 2016

Adsorbents

Data points

# Adsorbent Gas q / mol kg⁻¹ S / mol mol⁻¹ -ΔH / kJ mol⁻¹
546 CuBTC Methane/Hydrogen 1.12 19.0 None
547 [BMIM][BF4]/CuBTC (5 wt%) Methane/Hydrogen 1.12 20.0 None
548 [BMIM][BF4]/CuBTC (20 wt%) Methane/Hydrogen 1.12 26.0 None
549 [BMIM][BF4]/CuBTC (30 wt%) Methane/Hydrogen 1.12 26.0 None
1500 CuBTC Carbon dioxide/Methane 5.58 5.52 None
1501 [BMIM][BF4]/CuBTC (5 wt%) Carbon dioxide/Methane 5.35 5.2 None
1502 [BMIM][BF4]/CuBTC (20 wt%) Carbon dioxide/Methane 4.37 4.2 None
1503 [BMIM][BF4]/CuBTC (30 wt%) Carbon dioxide/Methane 3.12 3.55 None
2154 CuBTC Carbon dioxide/Hydrogen 5.58 110.0 None
2155 [BMIM][BF4]/CuBTC (5 wt%) Carbon dioxide/Hydrogen 5.35 108.0 None
2156 [BMIM][BF4]/CuBTC (20 wt%) Carbon dioxide/Hydrogen 4.37 108.0 None
2157 [BMIM][BF4]/CuBTC (30 wt%) Carbon dioxide/Hydrogen 3.12 90.0 None
3230 CuBTC Carbon dioxide/Nitrogen 5.58 16.0 None
3231 [BMIM][BF4]/CuBTC (5 wt%) Carbon dioxide/Nitrogen 5.35 15.5 None
3232 [BMIM][BF4]/CuBTC (20 wt%) Carbon dioxide/Nitrogen 4.37 14.0 None
3233 [BMIM][BF4]/CuBTC (30 wt%) Carbon dioxide/Nitrogen 3.12 12.0 None