Supporting Information for Capture of H2S from Binary Gas Mixture by Imidazolium-Based Ionic Liquids with Non-Fluorous Anions: A Theoretical Study Jie-Jie Chen, Wen-Wei Li, and Han-Qing Yu* Department of Chemistry, University of Science & Technology of China, Hefei, 230026, China Xue-Liang Li* School of Chemical Engineering, Hefei University of Technology, Hefei, 230009, China *Corresponding authors: Prof. Xue-Liang Li, E-mail: lixuel987@163.com; Prof. Han-Qing Yu, E-mail: hqyu@ustc.edu.cn 1 Interaction energy of ion-H2S In the geometry optimization, the positions of all the atoms were fully relaxed by using DMol3 code. To say, the structure with the most negative energy was investigated to compare with the other system. The true minima in the potential energy surface were confirmed in details. For example, the geometry structures of the possible local minimums for the [bmim]-H2S system are shown in Figure S1(a-1~a-4). The structure in Figure S1(a-4) with the strongest interaction energy was used to analyze the topological characteristics in this study. The changing trend of the values of ΔEI-S, PW91/DNP, ΔEI-S, PW91/TNP and ΔEI-S, PBE/TNP in Table S1 separately based on basis levels of PW91/DNP, PW91/TNP and PBE/TNP is identical to each other. Thus, the most stable structure (i.e., most negative energy) of each cation-H2S system has been obtained and is shown in Figure S1. The negative values of the cation-H2S interaction energy shown in Table S1 indicate that the systems tend to be stable with the absorption of H2S. These suggest that the H2S molecule prefers to approach from the S atom toward the C2H hydrogen for the cation of [bmim] and [hbmim] correspondingly shown in Figure S1(a-4) and (c-4). But the most stable interaction site of [bhmim] and H2S is between the H2S and hydroxyl group on methyl of imidazolium. The C2H hydrogen, which is the hydrogen attached to the carbon atom positioned between the two nitrogen atoms of the imidazolium ring, carries the most positive charge in the cation. Gas solubility calculations 2 Many reported results show that the imidazolium-based ILs have a considerable solubility capacity of H2S, even greater than that of CO2.1-4 The solubility of gases in solvents is quantified by using Henry’s law. For instance, Henry’s law constant (KH) for the solubilities of H2S and CO2 in a common IL, [bmim][PF6], are 0.1435 and 5.176 MPa at 298.15 K, respectively. This large difference in Henry’s law constant suggests that it may be possible to selectively capture and separate these gases using ILs. Higher KH values of H2S in the imidazolium-based ILs reported by Karadas et al.7 prove the capacity of imidazolium ILs for absorbing H2S. The gas solubilities in these six ILs have been calculated by conductor-like screening model for real solvents (COSMO-RS) method.8 The COSMO-RS developed by Klamt et al.9 provides an alternative approach to predict the thermodynamic properties of fluids for various systems, including ILs.10-11 All COSMO-RS calculations were computed at the BP/TZP level. The available studies on the predictive ability of the COSMO-RS model for gas solubilities in ILs have proven to be successful. For instance, the calculated KH of CO2 in [bmim][PF6] and [bmim][BF4] around ambient temperature reported by Zhang et al.12 agree with the experimental data well. Therefore, the COSMO-RS method can be used to predict the H2S solubility in these ILs at ambient temperature. The calculated KH of H2S and CO2 in these six ILs separately in Table 2 and Table S2 indicate that the solubility of H2S is higher than that of CO2 in imidazolium-based ILs. If we know the density of ILs, the calculated KH in the unit of 3 mol/(L·atm) can be transferred to that in pressure (MPa, bar, atm) as described in the following equation: 0.1 cIL (mol/L ) 100 IL (g/cm 3 ) K H (MPa ) K H (mol/L atm ) K H (mol/L atm ) M IL (g/mol ) (S1) Then, the calculated KH values in Table 2 and Table S2 can be compared with those in pressure from some references.5-6,12 For example, the density of [bmim]MeSO4 is 1.21 g/cm3, and the KH for H2S and CO2 in this IL are 0.470 and 5.983 MPa, respectively, from Equation S1. The magnitude order is the same with the experimental data5-6 in [bmim][PF6]. 4 Table S1. Interaction energy (EI-S, kcal/mol) of ions in NIILs and H2S calculated at different basis levels of PW91/DNP, PW91/TNP and PBE/TNP according to the geometry structures of the possible local minimums for the ion-H2S systems in Figure S1 Ions ΔEI-S,PW91/DNP ΔEI-S,PW91/TNP ΔEI-S,PBE/TNP (a-1) [bmim]-H2S-1 -11.585 -5.977 -4.822 (a-2) [bmim]-H2S-2 -12.344 -8.423 -7.242 (a-3) [bmim]-H2S-3 -12.734 -8.732 -6.826 (a-4) [bmim]-H2S-4 -13.359 -9.277 -8.488 (b-1) [bhmim]-H2S-1 -17.420 -12.929 -11.592 (b-2) [bhmim]-H2S-2 -14.146 -9.235 -8.052 (b-3) [bhmim]-H2S-3 -11.883 -7.962 -6.680 (b-4) [bhmim]-H2S-4 -16.382 -12.318 -8.649 (c-1) [hbmim]-H2S-1 -12.580 -8.346 -7.988 (c-2) [hbmim]-H2S-2 -14.107 -9.592 -8.594 (c-3) [hbmim]-H2S-3 -16.357 -11.778 -8.268 (c-4) [hbmim]-H2S-4 -16.529 -11.986 -9.168 (c-5) [hbmim]-H2S-5 -12.783 -8.265 -6.759 (e) LAC-H2S -21.181 -17.328 -16.658 (f) MeSO4-H2S -13.241 -10.248 -10.079 5 Table S2. The Henry’s law constants of CO2 in the imidazolium-based ILs predicted by COSMO-RS at 298.15 K ILs KH (mol/(L·atm)) [bmim]MeSO4 0.0808 [bmim]LAC 0.0567 [bhmim]MeSO4 0.0451 [bhmim]LAC 0.0507 [hbmim]MeSO4 0.0512 [hbmim]LAC 0.0591 6 Table S3. Interaction energy (EA-C, kcal/mol) of cation and anion in NIILs calculated at different basis levels of PW91/DNP, PW91/TNP and PBE/TNP for different anion sites relative to cation according to Figure S2 NIILs ΔEA-C,PW91/DNP ΔEA-C,PW91/TNP ΔEA-C,PBE/TNP (a-1) [bmim]LAC-1 -89.584 -94.866 -89.236 (a-2) [bmim]LAC-2 -97.327 -99.419 -97.032 (b-1) [bmim]MeSO4-1 -87.361 -86.802 -85.864 (b-2) [bmim]MeSO4-2 -94.192 -93.424 -91.763 (c-1) [bhmim]LAC-1 -96.390 -97.313 -91.399 (c-2) [bhmim]LAC-2 -118.823 -120.032 -110.627 (d-1) [bhmim]MeSO4-1 -90.095 -89.478 -85.372 (d-2) [bhmim]MeSO4-2 -104.966 -102.331 -102.775 (e-1) [hbmim]LAC-1 -93.155 -93.349 -91.388 (e-2) [hbmim]LAC-2 -101.752 -101.573 -99.743 (f-1) [hbmim]MeSO4-1 -92.336 -91.224 -89.114 (f-2) [hbmim]MeSO4-2 -100.480 -98.946 -97.539 7 Table S4. Interaction energy (EIL-S, kcal/mol) between NIIL and H2S with hydrogen bonding calculated at different basis levels of PW91/DNP, PW91/TNP and PBE/TNP for different H2S sites relative to NIIL according to Figure 2 NIIL-H2S ΔEIL-S,PW91/DNP ΔEIL-S,PW91/TNP ΔEIL-S,PBE/TNP (a-1) [bmim]LAC-H2S-1 -24.102 -19.245 -12.736 (a-2) [bmim]LAC-H2S-2 -23.296 -17.124 -12.179 (b-1) [bmim]MeSO4-H2S-1 -21.342 -18.393 -15.020 (b-2) [bmim]MeSO4-H2S-2 -19.371 -16.235 -13.834 (c-1) [bhmim]LAC-H2S-1 -12.753 -6.689 -9.745 (c-2) [bhmim]LAC-H2S-2 -11.382 -6.278 -9.322 (d-1) [bhmim]MeSO4-H2S-1 -19.286 -17.718 -13.154 (d-2) [bhmim]MeSO4-H2S-2 -18.372 -17.595 -7.320 (e-1) [hbmim]LAC-H2S-1 -25.376 -19.213 -15.805 (e-2) [hbmim]LAC-H2S-2 -22.225 -11.803 -11.376 (f-1) [hbmim]MeSO4-H2S-1 -17.646 -14.707 -9.912 (f-2) [hbmim]MeSO4-H2S-2 -16.029 -9.483 -8.143 8 Table S5. Interaction energy (EIL-M, kcal/mol) between NIIL and CH4 with hydrogen bonding calculated at different basis levels of PW91/DNP, PW91/TNP and PBE/TNP for different CH4 sites relative to NIIL NIIL-CH4 ΔEIL-M,PW91/DNP ΔEIL-M,PW91/TNP ΔEIL-M,PBE/TNP (a-1) [bmim]LAC-CH4-1 -13.623 -13.095 -4.765 (a-2) [bmim]LAC-CH4-2 -11.373 -7.788 -2.198 (b-1) [bmim]MeSO4-CH4-1 -18.327 -18.677 -10.381 (b-2) [bmim]MeSO4-CH4-2 -15.651 -15.572 -9.902 (c-1) [bhmim]LAC-CH4-1 -9.477 -8.181 -3.797 (c-2) [bhmim]LAC-CH4-2 -5.170 0.245 -2.613 (d-1) [bhmim]MeSO4-CH4-1 -14.147 -10.463 -2.565 (d-2) [bhmim]MeSO4-CH4-2 -4.285 -6.861 -2.462 (e-1) [hbmim]LAC-CH4-1 -13.205 -15.604 -4.846 (e-2) [hbmim]LAC-CH4-2 -6.209 -9.483 -3.545 (f-1) [hbmim]MeSO4-CH4-1 -9.668 -10.471 -4.954 (f-2) [hbmim]MeSO4-CH4-2 -7.237 -7.675 -3.665 9 Figure S1. Geometry structures of the possible local minimums for the ion-H2S systems and with the interaction energy in Table S1 10 Figure S2. Geometry structures of NIILs for different anion sites relative to cation and with the interaction energy in Table S3 11 Figure S3. Geometry structures of NIILs for different CH4 sites relative to NIILs and with the hydrogen bond length in Angstrom and the interaction energy shown in Table S5 12 Figure S4. Relationship between log(MSD) and log(t) for the NIIL-H2S-CH4 systems: (a) [bmim]MeSO4; (b) [bmim]LAC; (c) [bhmim]MeSO4; (d) [bhmim]LAC; (e) [hbmim]MeSO4; and (f) [hbmim]LAC 13 Literature Cited 1. Pomelli CS, Chiappe C, Vidis A, Laurenczy G, Dyson PJ. Influence of the interaction between hydrogen sulfide and ionic liquids on solubility: Experimental and theoretical investigation. J Phys Chem B. 2007;111(45):13014-13019. 2. Shiflett MB, Yokozeki A. Separation of CO2 and H2S using room-temperature ionic liquid [bmim][PF6]. Fluid Phase Equilib. 2010;294(1-2):105-113. 3. Jalili AH, Rahmati-Rostami M, Ghotbi C, Hosseini-Jenab M, Ahmadi AN. 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J Phys Chem A. 1998;102(26):5074-5085. 10. Diedenhofen M, Eckert F, Klamt A. Prediction of infinite dilution activity coefficients of organic compounds in ionic liquids using COSMO-RS. J Chem Eng Data. 2003;48(3):475-479. 11. Bernales VS, Marenich AV, Contreras R, Cramer CJ, Truhlar DG. Quantum mechanical continuum solvation models for ionic liquids. J Phys Chem B. 2012;116(30):9122-9129. 12. Zhang XC, Liu ZP, Wang WC. Screening of ionic liquids to capture CO2 by COSMO-RS and experiments. AIChE J. 2008;54(10):2717-2728. 15 Table of Contents (TOC) art A computational investigation into the interactions between H2S and NIILs with different combinations of imidazolium cations and non-fluorous anions for effective H2S capture from H2S-CH4 mixture. 16