Novel Inverse Supported Ionic Liquid Absorbents for Acidic Gas Removal from Flue Gas

被引:15
作者
Karousos, D. S. [1 ]
Kouvelos, E. [1 ]
Sapalidis, A. [1 ]
Pohako-Esko, K. [2 ]
Bahlmann, M. [2 ]
Schulz, P. S. [2 ]
Wasserscheid, P. [2 ]
Siranidi, E. [1 ]
Vangeli, O. [1 ]
Falaras, P. [1 ]
Kanellopoulos, N. [1 ]
Romanos, G. Em. [1 ]
机构
[1] NCSR Demokritos, INN, 153 10 Aghia Paraskevi Attikis, Athens, Greece
[2] Univ Erlangen Nurnberg, Lehrstuhl Chem Reakt Tech, Egerlandstr 3, D-91058 Erlangen, Germany
关键词
SELECTIVE CHEMICAL-SEPARATION; CARBON-DIOXIDE; REVERSIBLE CAPTURE; POROUS MATERIALS; EFFICIENT SO2; CO2; CAPTURE; ABSORPTION; TEMPERATURE; SOLUBILITY; TRICYANOMETHANIDE;
D O I
10.1021/acs.iecr.6b00664
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work reports on the astonishing high capacity of inverse supported ionic liquid absorbents, hereinafter denoted as "inverse SILPs" to remove acidic gases (SO2 and CO2) from flue gas streams. These nonconventional SILPs are easily prepared in the form of flowing powder via a phase inversion technique and consist of tiny ionic liquid (IL) droplets enclosed into an ultrathin, porous solid sleeve of pyrogenic silica nanoparticles. The CO2/N-2 and SO2/CO2 separation performance and regeneration efficiency of inverse SILPs developed from six different ILs and two IL/chitosan ionogels was examined via gravimetric CO2, N-2 absorption isotherms and via SO2, CO2, O-2 breakthrough curves from gas mixtures in fixed beds. The involved ILs varied from chemisorbing ones, composed of alkyl- or alkanol-ammonium cations and amino acid anions, to physisorbing ones including ether functionalized anions and 1-alky1-3-methylimidazolium cations. It is noteworthy that the best performing inverse SILP consisted of a very common IL, the 1-butyl-3-methylimidazolium chloride [BMIM] [Cl], the absorption capacity of which was slightly enhanced by dissolving 5 wt % of chitosan to form the respective ionogel. The material's performance was stable in repeated cycles of absorption and regeneration at 60 degrees C under helium flow, exhibiting SO2/CO2 selectivity of above 300, while the SO2 and CO2 absorption capacity was 1.6 and 0.6 mmol/g respectively at 25 degrees C, in a gas stream of 1 bar composed of 0.13 vol % SO2, 13 vol % CO2, 11.5 vol % O-2 and N-2 (balance).
引用
收藏
页码:5748 / 5762
页数:15
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