Prediction and verification of heat capacities for pure ionic liquids

Prediction and verification of heat capacities for pure ionic liquids

Journal Pre-proofs Full Length Article Prediction and verification of heat capacities for pure ionic liquids Zhengxing Dai, Yifeng Chen, Chang Liu, Xi...

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Journal Pre-proofs Full Length Article Prediction and verification of heat capacities for pure ionic liquids Zhengxing Dai, Yifeng Chen, Chang Liu, Xiaohua Lu, Yanrong Liu, Xiaoyan Ji PII: DOI: Reference:

S1004-9541(20)30693-5 https://doi.org/10.1016/j.cjche.2020.10.040 CJCHE 2072

To appear in:

Chinese Journal of Chemical Engineering

Received Date: Revised Date: Accepted Date:

22 September 2020 19 October 2020 28 October 2020

Please cite this article as: Z. Dai, Y. Chen, C. Liu, X. Lu, Y. Liu, X. Ji, Prediction and verification of heat capacities for pure ionic liquids, Chinese Journal of Chemical Engineering (2020), doi: https://doi.org/10.1016/ j.cjche.2020.10.040

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© 2020 The Chemical Industry and Engineering Society of China, and Chemical Industry Press.

Chinese Journal of Chemical Engineering (Template) Title of the paper. Prediction and verification of heat capacities for pure ionic liquids Author names and affiliations. Zhengxing Dai,1 Yifeng Chen,1 Chang Liu,1 Xiaohua Lu,1 Yanrong Liu,2,3,* Xiaoyan Ji2,* 1State Key Laboratory of Material-Oriented Chemical Engineering, Nanjing Tech University,

Nanjing, China 2Energy Engineering, Division of Energy Science, Luleå University of Technology, Luleå, Sweden 3Swerim AB, Box 812, SE-97125 Luleå, Sweden Corresponding author. Tel/Fax: +46 920 492837; E-mail: [email protected] Tel: +46 370 635443; E-mail: [email protected] Abstract. The heat capacity of ionic liquids is an important physical property, and experimental measuring is usually used as a common method to obtain them. Owing to the huge number of ionic liquids that can be potentially synthesized, it is desirable to acquire theoretical predictions. In this work, the Conductor-like Screening Model for Real Solvents (COSMORS) was used to predict the heat capacity of pure ionic liquids, and an intensive literature survey was conducted for providing a database to verify the prediction of COSMO-RS. The survey shows that the heat capacity is available for 117 ionic liquids at temperatures ranging 77.66-520 K since 2004, and the 4025 data points in total with the values from 76.37 to 1484 J·mol-1·K-1 have been reported. The prediction of heat capacity with COSMO-RS can only be conducted at two temperatures (298 and 323 K). The comparison with the experimental data proves the prediction reliability of COSMO-RS, and the average relative deviation (ARD) is 8.54%. Based on the predictions at two temperatures, a linear equation was obtained for each ionic liquid, and the heat capacities at other temperatures were then estimated via interpolation and extrapolation. The acquired heat capacities at other temperatures were then compared with the experimental data, and the ARD is only 9.50%. This evidences that the heat capacity of a pure ionic liquid follows a linear equation within the temperature range of study, and COSMO-RS can be used to predict the heat capacity of ionic liquids reliably.

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Keywords. Ionic liquids; Heat capacity; COSMO-RS Graphical abstract

Highlights. 

4025 experimental data points of heat capacity of 117 ionic liquids were collected at temperature range of 77.66-520 K.



COSMO-RS was used to predict heat capacities of collected ionic liquids at 298 and 323 K.



Temperature-dependent linear correlations of heat capacity were obtained and applied for predicting heat capacity at temperatures other than 298 and 323 K.



The results evidenced that COSMO-RS can effectively predict the heat capacity of ionic liquids.

1. Introduction Ionic liquid (IL) is an emerging “green solvent” with the merits of immeasurably low vapor pressure, excellent chemical and thermal stability, wide electrochemical window, nonflammability, and tunable properties [1]. It has been widely developed in many research fields, such as gas capture/separation and conversion [2-4], biomaterial dissolution [5], battery [6], and absorption heat transformers [7]. Due to the super tunable properties, 1018 kinds of ILs can be potentially formed through the combination of different anions and cations, resulting in different properties (e.g., density, viscosity, heat capacity, surface tension, CO2 solubility) and leading to their applications in a variety of areas. Heat capacity is one of the important properties and also an indispensable parameter when estimating the energy balance in the processes with temperature as variable [8]. The

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assessment of their values is essential for the reasonable tailoring of solvent properties. For example, ILs with low heat capacities are favorable in the CO2 separation and absorption heat transformers because of low energy requirements [9]. Compared with other properties, such as density, viscosity, surface tension, and CO2 solubility, the study on heat capacity is insufficient [9]. Measuring heat capacity with experimental techniques is not only costly but also impractical due to the large number of ILs. Therefore, it is essential to predict the heat capacities of ILs with theoretical methods and models. Several articles on modeling the heat capacity of ILs have been published, and in general, adjustable parameters are needed. For instance, Müller et al. developed a model based on the temperature-dependent heat capacities of the constituent ions for each IL, and the parameters for 39 cations and 29 anions were obtained based on 104 ILs with 2443 data points, making it possible to predict the heat capacity of 1248 pure ILs [10]. A deviation lower than 7.2% was acquired when modeling the ILs not used in parameter fitting at temperatures up to 425.15 K. Ge et al. combined the Joback group contribution (GC) method with the principle of corresponding states [11] to predict the heat capacity of ILs, and the GC parameters for three new groups of -SO-, B, and P were obtained. The developed model was used to predict the heat capacities of other ILs (51 ILs with 961 data points in a temperature range of 256470 K), showing a 2.9% deviation [12]. Later, the method was used to predict the heat capacity of 3-(alkoxymethyl)-1H-imidazolium salicylate ([H-Im-C1OCn][Sal], n = 3-11) up to 323.15 K by Jacquemin et al. [13], and a deviation about 3.2% was acquired. Sattari et al. [14] combined the GC method and genetic function approximation to predict the heat capacities, and the best prediction is for the dialkyl imidazolium-based ILs (ARD = 1.51%), while the worst is for the phosphonium-based ILs (3.65%). Soriano et al. developed a groupadditivity model with three adjustable parameters [15], and a deviation of 0.69% was achieved for 32 imidazolium-, pyridinium-, and pyrrolidinium-based ILs. The extreme learning machine (ELM, 6 parameters) [16], multiple linear regression (MLR, 5 parameters), and artificial neural network (ANN, 5 parameters) were used to predict the heat capacity of imidazolium-, pyridinium-, pyrrolidinium-, and phosphonium-based ILs for comparison [8]. It was found that ELM (ARD = 0.44%) is the best, followed by ANN (ARD = 0.64%) and MLR (ARD = 2.72%). Three chemical structural models (7 parameters), i.e., coupled simulated annealing optimization algorithm (CSA-LSSVM), gene expression programming (GEP), and adaptive-neuro fuzzy inference system (ANFIS) optimized by the hybrid method (Hybrid-ANFIS), were also used for predicting the heat capacity of 56 ILs [17], evidencing that CSA-LSSVM (0.9%) is better than Hybrid-ANFIS (1.74%) and GEP (2.31%). Recently, Conductorlike Screening Model for Real Solvents (COSMO-RS) has been

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strongly recommended for predicting the thermodynamic properties of ILs, as the molecular structural information is the only required input [18]. As a prior and a rapid screening method, COSMO-RS has evidenced its prediction capability for the solubility (i.e., cellulose, keratin, gas) [5,19,20], activity coefficient [21], Henry’s constant [22], viscosity [23], and density [24] of ILs. However, to the best of our knowledge, no research work has ever been conducted to investigate the prediction capacity of COSMO-RS for the heat capacities of ILs as well as its prediction reliability. To fulfill this gap, in this work, the heat capacity of ILs was predicted with COSMORS, combined with the verification for both COSMO-RS predictions and their further linear correlations. A comprehensive survey of the experimental heat capacities of ILs was firstly carried out. COSMO-RS was used to predict the heat capacity of ILs at 298 and 323 K, and the predictions were compared with the experimental results for verification. Further, temperature-dependent linear correlations were obtained based on the results from COSMORS and then used to estimate the heat capacities at other temperatures, and the comparison with experimental results was also conducted for verification. 2. Computational Details COSMO-RS calculations were performed using the software COSMOtherm (version 19.0.4, revision 5528, applied with parameterization BP_TZVP_19, COSMOlogic, Leverkusen, Germany), followed by the reported standard methods [25]. All of the ILs were implemented in COSMOtherm software following the electroneutral approach, i.e., each IL was treated as a separated cation and anion. To use COSMO-RS, the COSMOfiles for all the studied IL-cations and anions are needed. In this work, those (1) for the IL cations of [1B3Mpy]+, [1B4Mpy]+, [BAPY]+, [BENBIM]+, [BENMIM]+, [BIPIM]+, [BPDM] +, [BPHENIM]+, [BPIM]+, [C3MPIP]+, [C3MPy]+, [C3MPyrr]+, [C9MIM]+,

[COPBIM]+,

[EAPY]+,

[EMPIP]+,

[EMPyrr]+,

[HAPY]+,

[HOEtDMHA]+, [HOMEA]+, [N4441]+, [N7777]+, [N8888]+, and [P66614]+; (2) for the IL anions of [1122FSO3]−, [AESO3]−, [C2COO]−, [C3COO]−, [C4COO]−, [C6SO4]−, [Cys]−, [Deca]−, [MDEGSO4]−, [EtSO4]−, [HexO]−, [Lys]−, [OctO]−, [Oph]−, [Pro]−, [Ser]−, [Thr]−, [Tos]−, and [Val]−, were calculated based on the procedures described in the computation details [25]. The COSMOfiles for other IL-ions studied in this work were taken from the COSMO-RS database. The full and abbreviation names, the structures of cations and anions, as well as the COSMO-RS sigma surfaces are given in Tables S1 and S2.

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By using COSMO-RS, the heat capacity of ILs can be acquired at 298 and 323 K. Then, a temperature-dependent linear equation was obtained for each IL, making it possible to estimate the heat capacity at different temperatures theoretically. The prediction results from COSMO-RS and those estimated with the obtained linear correlations were verified by comparing with the experimental heat capacities. The ARDs were calculated to quantify the model performance, and the expression is defined as 𝑵𝑷

( ) ∑│(𝑪

𝟏𝟎𝟎 ( 𝑨𝑹𝑫% = 𝑵𝑷 ×

𝑬𝒙𝒑. 𝑷

― 𝑹𝑺 ― 𝑪𝑪𝑶𝑺𝑴𝑶 )/𝑪𝑬𝒙𝒑. 𝒑 𝑷 │)

𝒊=𝟏

― 𝑅𝑆 where 𝐶𝐶𝑂𝑆𝑀𝑂 is the heat capacity predicted by COSMO-RS or estimated with the 𝑝

linear correlation. 3. Results and Discussion 3.1. Literature survey A comprehensive survey was conducted based on open publications since 2004. 4025 experimental data points for 117 ILs (including imidazolium-, pyridinium-, pyrrolidinium-, morpholinium-, piperidinium-, ammonium-, phosphonium-based) at temperatures ranging from 77.67 to 520 K were collected and used as the database for verifying the performance of COSMO-RS. The detailed results of the database are displayed in Tables 1 and S3, as well as Fig. 1. Among these 117 ILs, for the ILs of [BMIM][Cl], [BMMIM][BF4], [BMMIM][PF6], and [PMMIM][Tf2N], only two experimental data points were reported at 298 and 323 K, respectively (Table 1.). 1600

[P66614][FeCl4]: maximum 1484 J·mol-1·K-1

Heat capacity/J·mol-1·K-1

1400 1200 1000 800 600 400 200 0

[EPy][Br]: minimum 76.37 J·mol-1·K-1

100

200

300

400

500

Temperature/K

Fig. 1. Experimental heat capacities at different temperatures. Table 1. ILs studied in this work. No.

ILs

T/K

Cp/J·mol-1·K-1

Data points

Ref.

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1 2

[1B3MPy][BF4] [1B4MPy][BF4]

3

[BAPy][Tf2N]

4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43

[BENBIM][Tf2N] [BENMIM][1122FSO3] [BENMIM][BF4] [BENMIM][PF6] [BENMIM][Tf2N] [BIPIM][Tf2N] [BMIM][BF4] [BMIM][CF3COO] [BMIM][Cl] [BMIM][DCA] [BMIM][FeCl4] [BMIM][I] [BMIM][MeSO4] [BMIM][NO3] [BMIM][OAc] [BMIM][OSO4] [BMIM][OTf] [BMIM][Oph] [BMIM][Tf2N] [BMIM][Tos] [BMIM][FAP] [BMMIM][FAP] [BMMIM][BF4] [BMMIM][PF6] [BMMIM][Tf2N] [BMPy][OTf] [BMPyrr][OTf] [BMPyrr][Tf2N] [BMPy][Tf2N] [BPDMIM][Tf2N] [BPHENIM][Tf2N] [BPIM][Tf2N] [Bpy][BF4] [Bpy][Tf2N] [BTMA][Tf2N] [C10MIM][Oph] [C10MIM][Tf2N] [C14MIM][Tf2N] [C3MIM][Br] [C3MIM][Tf2N]

278.15-328.15 278.15-328.15 313.13-423.14, 298-343 303.1-343.1 273.41-309.14 278.51-324.46 258.09-355.09 258.09-355.09 293.15-348.15 283.15-323.15 187.91-368.36 298.15, 323.15 235.8-367.14 308.16-423.22 209.86-368.43 293.2-358.2 271.8-368.19 253.15-413.15 298.15-343.15 292.86-367.78 303.15-353.15 283.15-328.15 152.77-343.89 273.15-413.15 283.15-338.15 298.15, 323.15 298.15, 323.15 293.15-323.15 323.1-353.1 293.15-338.15 241.39-368.4 293.1-333.1 294.15-348.15 303.1-343.1 293.15-348.15 290-390 323.18-423.15 278.32-367.93 303.15-353.15 277.33-370 295.86-304.97 222.57-368.28 293.15-333.15

402-427 403.1-429.4

21 21

[26] [26]

688-732, 611-648

23, 10

[27,28]

556-591 381-457 288-337 321-411 588-641 682-724 360.2-377.3 367.8-441.7 322.7, 333.7 355.9-403.2 436-471 287.7-336.4 477.11-400.51 345.1-382.3 360-470 635-698 425-465 430.2-464.9 558.99-584.36 238.4-458.7 664-807 748.2-799.6 375.3, 406.5 433.6, 449.1 588-608 464-496 439.9-464.6 549-638 541-582 693-735 628-662 684-724 379.16-428.45 592-635 547.5-600.9 624-671 739.7-813.4 1130-1154 260-306.3 482-514

9 14 20 40 39 56 9 359 2 80 24 116 14 83 21 46 40 11 10 22 10 12 2 2 10 31 12 73 41 55 9 56 22 21 49 11 12 14 72 41

[29] [30] [30] [30] [30] [31] [32] [33] [34] [35] [36] [37] [38] [39] [40] [41] [35] [42] [43] [44] [45] [46] [34] [34] [47] [48] [46] [35] [48] [31] [29] [31] [49] [28] [35] [42] [50] [50] [35] [51]

6

44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76

[C3MPIP][Tf2N] [C3MPy][Br] [C3MPyrr][Tf2N] [C3MPy][Tf2N] [C3Py][BF4] [C3Py][PF6] [C9MIM][PF6] [COPBIM][Tf2N] [EAPy][Tf2N] [EEIM][EtSO4] [EMIM][BF4] [EMIM][C(CN)3] [EMIM][C6SO4] [EMIM][DCA] [EMIM][DEP] [EMIM][EtSO4] [EMIM][MDEGSO4] [EMIM][OAc] [EMIM][OTf] [EMIM][Oph] [EMIM][SCN] [EMIM][TCB] [EMIM][Tf2N] [EMMIM][Tf2N] [EMMor][EtSO4] [EMPIP][EtSO4] [EMPyrr][EtSO4] [EMPy][Tf2N] [Epy][Br] [Epy][PF6] [Epy][Tf2N] [EtOMMPyrr][FAP] [EtOMMPyrr][Tf2N]

77

[HAPy][Tf2N]

78 79 80 81 82 83 84 85 86

[HDMIM][Tf2N] [HMIM][BF4] [HMIM][BOB] [HMIM][DCA] [HMIM][OTf] [HMIM][PF6] [HMIM][Oph] [HMIM][Tf2N] [HOEtDMHA][Br]

298-520 220-370 283.15-358.15 293.1-333.1 278.15-338.15 80.68-359.46 263.14-355.13 293.15-348.15 313.12-423.17 293.15-323.15 283.15-323.15 293.15-323.15 283.15-338.15 303.2-358.2 298-343 196.36-389.95 303.2-358.2 303.15-393.35 303.2-358.2 303.15-353.15 293.15-323.15 293.15-363.15 283.15-338.15 293.15-323.15 288.15-383.15 288.15-383.15 288.15-383.15 293.1-333.1 77.66-359.92 85.82-360.87 288.15-338.15 283.15-338.15 283.15-338.15 313.15-418.13, 298-343 298-368.55 283.15-323.15 239.33-397.44 293.15-333.15 298-423.17 258.058-355.136 303.15-353.15 288.72-350.36 298.22-339.42

607-756 258.4-307 544.2-594 510-549 352-385 132.69-394.4 544.3-610 649-690 619-649 411-428 300.2-314.4 338-348 505.2-537.6 328-354 460-494 347-400 526.39-544.08 325.2-356.5 379-402 294.9-320.7 276-285 406.4-424.3 521-541.7 524-544 443-489 422-483 413-455 484-522 76.37-263.8 122.41-363.77 519-539 719.4-769.1 575.3-602.6

24 18 17 41 25 96 18 56 23 10 9 10 12 12 10 170 12 10 12 11 10 9 12 10 20 20 20 41 109 140 21 12 12

[52] [53] [54] [48] [55] [56] [30] [31] [27] [47] [32] [47] [46] [57] [27] [58] [57] [59] [57] [42] [47] [60] [46] [47] [61] [61] [61] [48] [62] [56] [63] [46] [46]

731-801, 663-712

22, 10

[27, 28]

972.6-1084 422.8-443.8 575.8-656.7 524-575 517-572 444.9-504.2 496.7-535 599-647 388.5-462

54 9 81 41 41 21 11 107 17

[50] [32] [64] [51] [51] [30] [42] [65] [66]

7

87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117

[HOMEA][C3COO] [HOMEA][C4COO] [HOMEA][C2COO] [N4441][AESO3] [N4441][Lys] [N4441][Ser] [N4441][Thr] [N7777][Br] [N8888][Br] [OMIM][BF4] [OMIM][Cl] [OMIM][OTf] [OMIM][PF6] [OMIM][Oph] [OMIM][Tf2N] [P4444][FAP] [P4444][AESO3] [P4444][Cys] [P4444][Lys] [P4444][Pro] [P4444][Ser] [P4444][Thr] [P4444][Val] [P66614][FeCl4] [P66614][C3COO] [P66614][DCA] [P66614][Deca] [P66614][HexO] [P66614][OAc] [P66614][OctO] [PMMIM][Tf2N]

286.15-336.15 283.15-333.15 287.15-326.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 293.55-339.36 290-350 205.61-367.89 216.96-340.45 313.17-423.14 253.15-413.15 303.15-353.15 187.58-367.13 283.15-328.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 308.16-423.22 293.15-363.15 313.15-413.15 293.15-363.15 293.15-363.15 293.15-363.15 293.15-363.15 298.15, 323.15

357-385 385-421 323-336 822-892 817-925 632-681 748-821 754-876 865-1062 463.8-542.7 412-471.8 588-651 549-647 505-546 630.7-743.7 971-1049.8 990-1090 914-1020 990-1110 838-939 742-815 952-1100 744-811 1342-1481 1107-1196 1060-1240 1181-1296 1133-1235 1096-1173 1138-1247 554.5, 558.7

91 105 111 9 9 9 9 18 30 107 50 23 33 11 87 7 9 9 9 9 9 9 9 24 15 61 15 15 15 15 2

[67] [67] [67] [68] [68] [68] [68] [69] [69] [35] [70] [28] [71] [42] [72] [46] [68] [68] [68] [68] [68] [68] [68] [36] [73] [74] [73] [73] [73] [73] [34]

As shown in Fig. 1, almost for all the studied ILs, their heat capacities at different temperatures follow a linear equation. The minimum heat capacity acquired from the survey (76.37 J·mol-1·K-1) belongs to [Epy][Br] at 77.66 K, while the maximum (1484 J·mol-1·K-1) affiliates to [P66614][FeCl4] at 418.19 K. The heat capacities for other ILs within the studied temperature range are between these two values. Except the linearly temperature-dependent, three other characteristics for the collected heat capacities can be observed from Table S3, i.e., 1) anions has a significant effect on the heat capacities of ILs compared with cations. For example, 𝛥𝐶𝐸𝑥𝑝. between [BMIM][Tf2N] and [BMIM][OTF] is 138.57 J·mol-1·K-1 at 298 K, 𝑝 while, for different cations, it is 77.47 J·mol-1·K-1 between [BMIM][Tf2N] and [C3MIM][Tf2N] at the same temperature; 2) the heat capacity increases with increasing the

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alkyl chain length of cations, e.g., the heat capacity increases from 489 to 971.7 J·mol-1·K-1 for [C3~C14MIM][Tf2N], and it increases from 790 to 903 J·mol-1·K-1 for [N7777~N8888]Br at 298 K; 3) the heat capacity increases with increasing the number of alkyl chains in the imidazolium cation, but not for the pyridinium cation. For instance, for the heat capacity [BMMIM][Tf2N] (591.9 J·mol-1·K-1) > [BMIM][Tf2N] (566.47 J·mol-1·K-1), and [EMMIM][Tf2N] (527 J·mol-1·K-1) > [EMIM][Tf2N] (524.3 J·mol-1·K-1) at 298 K, however, [EMPy][Tf2N] (514 J·mol-1·K-1) < [EPy][Tf2N] ( J·mol-1·K-1) at 323 K. 3.2. Prediction and verification 3.2.1 COSMO-RS verification The heat capacities of 117 ILs were predicted with COSMO-RS at 298 and 323 K. The results are listed in Table S4. It was found that COSMO-RS can be used for qualitative prediction. The predictions are consistent with the experimental results on 1) linear temperature-dependence, 2) significant effect of anions than cations, 3) effect of alkyl chain length in cations. However, for the effect of the number of alkyl chains in cations, the prediction tendency is not always correct. For example, the prediction tendency is correct for [EMMIM][Tf2N] (518.10 J·mol-1·K-1) and [EMIM][Tf2N] (490.17 J·mol-1·K-1), but incorrect for [EMPy][Tf2N] (533.45 J·mol-1·K-1) and [EPy][[Tf2N] (506.12 J·mol-1·K-1). The comparison of the COSMO-RS predictions with the experimental results is illustrated in Fig. 2. An acceptable ARD of 8.54% was acquired, indicating that COSMO-RS can also be used for quantitative predictions. The contribution to the ARD is mainly from the phosphonium- (1.06-38.63%), ammonium- (9.55-29.36%) and imidazolium- (3.4-34.38%) based ILs, e.g., the ARDs for [P4444][AESO3] and [N4441][AESO3] are 38.63 and 29.36%, respectively, and it is 34.50% for [BENMIM][BF4] at 298 K. The detailed results listed in Table S4 indicate that about 71% ILs (85 to 119) have ARDs lower than 10%, and the best is for [EMIM][OAc] (ARD = 0.28%). This implies that COSMO-RS can be used for quantitative prediction for most of ILs. Fig. 3 shows 34 ILs with ARDs higher than 10%, and these ILs should be more beware when using COSMO-RS to predict their heat capacities. From Fig. 3 it can be found that the ILs with the ARDs greater than 10% mainly have the features of 1) phosphonium-based ILs, including cations of [P4444]+ and [P66614]+, and amino acid (e.g., [Thr]−, [Ser]−, [Cys]−, [Lys]−, [Pro]−, [Val]−) and [AESO3]− anions; 2) ammoniumbased ILs structure with cation of [N4441]+ and anions of [AESO3]−, [Thr]−, and [Lys]−; 3) big size imidazolium cations, e.g., [BENMIM]+ together with anions of [BF4]−, [PF6]−, and [Tf2N]−; 4) halogen anion-based ILs i.e., [EPy][Br], [C3MPy][Br], [C3MIM][Br], and [BMIM][I].

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[BMPy][Tf2N] [BMPyrr][OTf] [BMPyrr][Tf2N] [BPDMIM][Tf2N] [BPHENIM][Tf2N] [BPIM][Tf2N] [BPy][BF4] [BPy][Tf2N] [BTMA][Tf2N] [C10MIM][Oph] [C10MIM][Tf2N] [C14MIM][Tf2N] [C3MIM][Br] [C3MIM][Tf2N] [C3MPIP][Tf2N] [C3MPy][Br] [C3MPy][Tf2N] [C3MPyrr][Tf2N] [C3Py][BF4] [C3Py][PF6]

CpCOSMO-RS/J·mol-1·K-1

1400 1200 1000 800

[BMIM][BF4] [BMIM][CF3COO] [BMIM][Cl] [BMIM][DCA] [BMIM][FeCl4] [BMIM][I] [BMIM][MeSO4] [BMIM][NO3] [BMIM][Oac] [BMIM][OSO4] [C9MIM][PF6] [COPBIM][Tf2N] [EAPy][Tf2N] [EEIM][EtSO4] [EMIM][BF4] [EMIM][C(CN)3] [EMIM][C6SO4] [EMIM][DCA] [EMIM][DEP] [EMIM][EtSO4]

[BMIM][OTf] [BMIM][Tos] [BMIM][Oph] [BMIM][Tf2N] [BMIM][FAP] [BMMIM][FAP] [BMMIM][BF4] [BMMIM][PF6] [BMMIM][Tf2N] [BMPy][OTf]

[1B3MPy][BF4] [1B4MPy][BF4] [BAPy][Tf2N] [BENBIM][Tf2N] [BENMIM][1122FSO3] [BENMIM][BF4] [BENMIM][PF6] [BENMIM][Tf2N] [BIPim][Tf2N]

ARD = 8.54%

600 400 [HMIM][BF4] [HMIM][DCA] [HMIM][OTf] [HMIM][PF6] [HMIM][BOB] [HMIM][Oph] [HMIM][Tf2N] [HOEtDMHA][Br] [HOMEA][C3COO] [HOMEA][C4COO]

200 0

0

200

400

600

800

[HOMEA][C2COO] [N4441][AESO3] [N4441][Lys] [N4441][Ser] [N4441][Thr] [N7777][Br] [N8888][Br] [OMIM][BF4] [OMIM][Cl] [OMIM][OTf]

[P4444][Val] [P66614][FeCl4] [P66614][DCA] [P66614][OAc] [P66614][OctO] [P66614][C3COO] [P66614][Deca] [P66614][HexO] [PMMIM][Tf2N] [OMIM][PF6] [OMIM][Oph] [OMIM][Tf2N] [P4444][FAP] [P4444][AESO3] [P4444][Lys] [P4444][Pro] [P4444][Ser] [P4444][cys] [P4444][Thr]

[EMPyRR][EtSO4] [EMPy][Tf2N] [EPy][Br] [EPy][PF6] [EPy][Tf2N] [EtOMmpyrr][FAP] [EtOMmPyrr][Tf2N] [HAPy][Tf2N] [HDMIM][Tf2N] [EMIM][ MDEGSO4] [EMIM][Oac] [EMIM][OTf] [EMIM][SCN] [EMIM][Oph] [EMIM][TCB] [EMIM][Tf2N] [EMMIM][Tf2N] [EMMor][EtSO4] [EMPIP][EtSO4]

1000 1200 1400

-1 -1 CExp. p /J·mol ·K

Fig. 2. Experimental heat capacity vs. COSMO-RS prediction at 298 and 323 K. 40 35

ARD/%

30 25 20 15

[P 66 [ 61 [P C3M4][D [B 666 IM ec M 14 ] a] IM ][F [B ] e r] [C [M Cl4 [H e O [ 3Py SO ] M N ][ 4] EA 7 7 PF ][C77] 6] [H 3 [B D [BM CO r] [H [ MIM IM O] O EM ] ] M I [T [I] [B E M EN A ][ f2N ][C S ] M C [H IM[P4 4C N] O ][ 44 OO M 1 4] [C EA 122 [Va ] 14 ][ FS l] M C2 O I C 3 [C M] O ] 3 [ O [P M Tf2 ] 44 Py N 4 ][ ] [E 4][ Br [ p FA ] [H N44 y][P P] M 41 F6 I ][ ] [P M][ Ly 4 D s [B [N 44 C ] EN 44 4][ A] BI 41] Ser [B M] [Th ] M [T r] IM f2 [B EN [E ][T N] M py os [P IM ][B ] [E 444 ][P r] M 4] F6 I [ ] [N [P M] Pro 44 44 [O ] 41 44 ph ] [B [P ][AE[Ly ] EN 44 S s] M 4 4 O3 I ] ] [P [P4 M] [cys 44 44 [B ] 44 4] F4 ][A [T ] ES hr] O 3]

10

Fig. 3. The ILs with the ARDs higher than 10% where the heat capacity was predicted with COSMO-RS. In order to further illustrate the performance of COSMO-RS, [HMIM][Tf2N], [BMMIM][FAP], and [P4444][AESO3] were chosen as three representatives to show the minimum (0.22%), medium (8.58%), and maximum (38.63%) ARDs when compared with experimental results. It was further found that, as shown in Fig. 4, no matter the deviation is large or small, the temperature effect on the heat capacity (i.e., the slope of the heat capacity predicted with COSMO-RS) agrees well with the experimental observation. The investigation for other ILs not displayed in Fig. 4 also evidenced the same results. Therefore, COSMO-RS can be used to predict the temperature effect on the heat capacity of ILs.

10

1100

Heat capacity/Jmol-1K-1

Cp=1.43T+567.06

1000

Experimental [HMIM][Tf2N] Original COSMO-RS [HMIM][Tf2N] Experimental [BMMIM][FAP] Original COSMO-RS [BMMIM][FAP] Experimental [P4444][AESO3] Original COSMO-RS [P4444][AESO3]

900 Cp=0.92T+490.05

800

Cp=1.00T+397.10

700

Cp=0.82T+357.23

Cp=0.94T+327.52

600

Cp=0.94T+321.20

300

280

360

340

320

Temperature/K

Fig. 4. Experimental and predicted heat capacities for three ILs with minimum ([HMIM][Tf2N]), medium ([BMMIM][FAP]) and maximum ([P4444][AESO3]) ARDs, respectively. 3.2.2 Extension of COSMO-RS predictions Based on the predicted heat capacities at 298 and 323 K, a linear correlation was conducted for each IL. The linear equations for 117 ILs are displayed in Table S5. Using the linear equations, the heat capacity at other temperatures were then estimated and compared with the available experimental data. Due to the availability of experimental data at temperatures other than 298 and 323 K, the comparison can only be conducted for 113 ILs with 3826 data points. The comparison is summarized in Fig. 5, with details listed in Table S6. The comprehensive analysis of Table S6 shows that the correlated linear equations can be used to reliably estimate the heat capacity, being consistent with the performance of COSMO-RS combined with its reliable prediction on the temperature impact. 2000

[C9MIM][PF6] [COPBIM][Tf2N] [EAPy][Tf2N] [EEIM][EtSO4] [EMIM][BF4] [EMIM][C(CN)3] [EMIM][C6SO4] [EMIM][DCA] [EMIM][DEP] [EMIM][EtSO4] [BMIM][BF4] [BMIM][CF3COO] [BMIM][DCA] [BMIM][FeCl4] [BMIM][I] [BMIM][MeSO4] [BMIM][NO3] [BMIM][Oac] [BMIM][OSO4]

CpHeat capacity equations/J·mol-1·K-1

1800 1600 1400 1200

[BMPy][Tf2N] [BMPyrr][OTf] [BMPyrr][Tf2N] [BPDMIM][Tf2N] [BPHENIM][Tf2N] [BPIM][Tf2N] [BPy][BF4] [BPy][Tf2N] [BTMA][Tf2N] [C10MIM][Oph] [BMIM][OTf] [BMIM][Tos] [BMIM][Oph] [BMIM][Tf2N] [BMIM][FAP] [BMMIM][FAP] [BMMIM][Tf2N] [BMPy][OTf]

[C10MIM][Tf2N] [C14MIM][Tf2N] [C3MIM][Br] [C3MIM][Tf2N] [C3MPIP][Tf2N] [C3MPy][Br] [C3MPy][Tf2N] [C3MPyrr][Tf2N] [C3Py][BF4] [C3Py][PF6]

[1B3MPy][BF4] [1B4MPy][BF4] [BAPy][Tf2N] [BENBIM][Tf2N] [BENMIM][1122FSO3] [BENMIM][BF4] [BENMIM][PF6] [BENMIM][Tf2N] [BIPim][Tf2N]

ARD = 9.50%

1000 800 600 400

[HMIM][BF4] [HMIM][DCA] [HMIM][OTf] [HMIM][PF6] [HMIM][BOB] [HMIM][Oph] [HMIM][Tf2N] [HOEtDMHA][Br] [HOMEA][C3COO] [HOMEA][C4COO]

200 0

0

[HOMEA][C2COO] [N4441][AESO3] [N4441][Lys] [N4441][Ser] [N4441][Thr] [N7777][Br] [N8888][Br] [OMIM][BF4] [OMIM][Cl] [OMIM][OTf]

[P4444][Val] [P66614][FeCl4] [P66614][DCA] [P66614][OAc] [P66614][OctO] [P66614][C3COO] [P66614][Deca] [P66614][HexO] [OMIM][PF6] [OMIM][Oph] [OMIM][Tf2N] [P4444][FAP] [P4444][AESO3] [P4444][Lys] [P4444][Pro] [P4444][Ser] [P4444][cys] [P4444][Thr]

[EMPyRR][EtSO4] [EMPy][Tf2N] [EPy][Br] [EPy][PF6] [EPy][Tf2N] [EtOMmpyrr][FAP] [EtOMmPyrr][Tf2N] [HAPy][Tf2N] [HDMIM][Tf2N] [EMIM][ MDEGSO4] [EMIM][Oac] [EMIM][OTf] [EMIM][SCN] [EMIM][Oph] [EMIM][TCB] [EMIM][Tf2N] [EMMIM][Tf2N] [EMMor][EtSO4] [EMPIP][EtSO4]

200 400 600 800 1000 1200 1400 1600 1800 2000 -1 -1 CExp. p /J·mol ·K

Fig. 5. Experimental heat capacity vs. linear correlation prediction at temperatures

11

other than 298 and 323 K. For quantitative prediction, an ARD of 9.50% was obtained for the correlations (Fig. 5). Although the ARD is slightly larger than that of COSMO-RS (8.51%), this accuracy is within the acceptable range compared to the experimental uncertainty (10%) as reported by Müller et al.[10] The results listed in Table S5 further indicate that 74% (84 to 115) ILs have the ARDs lower than 10%, resulting in the best one (0.52%) for [BMPy][OTf]. Therefore, COSMO-RS can be used to predict and further estimate the heat capacity at different temperatures. Among the ILs with ARDs higher than 10% (Fig. 6), [Epy][Br] is the worst one (40.47%), and the ILs displayed in Fig. 6 are also those with the ARDs higher than 10% in the COSMO-RS prediction. 40

ARD/%

35 30 25 20 15

[B M

IM [H [BM ][M O [H ME IM eSO O A ][F 4] M ][ eC EA C3 l4 ] C ] [C [C2 OO 3 M CO ] [C [P Py O] 4 14 4 ][B M 44 r [H [ IM ][V ] O P4 ][T al] M 44 f EA 4 2 N ][ ][F ] [B [ C AP EN [H N44 4CO ] M M 41 O IM IM ][L ] ][1 ][ ys] 1 DC [B [P 22F A] EN 4 4 SO BI 4 4 ] 3 ] [ [N M][ Ser 4 4 Tf ] 4 2 [B [C 1][ N] EN 3 P Th y r [B MI ][P ] M M F6 Py ][P ] r F [E r][O 6] [P py] Tf ] [E 444 [PF M 4] 6] [E IM [Pr [N M ][O o] 44 IM p 41 ][S h] ][ C [B [P4 AE N] EN 4 4 SO M 4][ 3] I L [P M][ ys] 4 B [B 44 F4 M 4][ ] IM cy [P [P4 ][ s] 4 4 4 4 To 44 4][ s] ][A Th E r [E SO ] py 3] ][B r]

10

Fig. 6. ARDs more than 10% predicted by linear correlations. In conclusion, original COSMO-RS can be used to predict the heat capacity at 298 and 323 K reliably, and the linear correlation makes it possible to reliably estimate the heat capacity at other temperatures. 3.2.3 Comparison of COSMO-RS with other models Five

ILs

of

[EMIM][BF4],

[BMIM][BF4],

[HMIM][Tf2N],

[EMIM][Tf2N],

[HMIM][BF4], which have the same prediction temperature (323 K) with other models of GC, MLR, ELM, group-additivity were selected for the comparison. The comparison shown in Fig. 7 evidenced that COSMO-RS is the best one for [HMIM][Tf2N] and [HMIM][BF4] compared with the other four models, but the worst one for [EMIM][Tf2N]. Additionally, for [EMIM][BF4], COSMO-RS is only better than the GC model, While for [BMIM][BF4], COSMO-RS is only worse than the group-additivity model. However, it should be pointed out that for COSMO-RS, the only needed input is the molecular structural information.

12

Meanwhile, the prediction of COSMO-RS is always with the ARD less than 6%, while for other models, the ARD can be up to 22%. Therefore, it is strongly recommended to use

ARD/%

COSMO-RS for the prediction. 24 22 20 18 16 14 12 10 8 6 4 2 0

This work Ge et al. [12] Kang et al.(MLR) [16] Kang et al.(ELM) [16] Soriano et al. [15]

M [EMI

] F4] f2N] f2N] BF4] ][BF4 M][B IM][T [EMIM][T [HMIM][ [BMI [HM

Fig. 7. Comparison of ARDs for different models. 4. Conclusions In this work, a heat capacity database including 117 ILs with 4025 experimental data points at 77.66-520 K was established based on open publications since 2004. COSMO-RS was used to predict the heat capacity of ILs, and its performance was verified based on the established database. The literature survey indicates that experimental heat capacity at different temperatures follows a linear equation within the scope of 76.37-1484 J·mol-1·K-1. The prediction and comparison show that COSMO-RS can provide reliable prediction at 298 and 323 K, and approximately 8.54% ARDs was acquired, evidencing that COSMO-RS can be used for quantitative prediction of the ILs heat capacity at these two temperatures. Linear equations were acquired for 117 ILs based on the COSMO-RS predicted results at 298 and 323 K, and used to estimate the heat capacity at temperatures other than 298 and 323 K. 3826 experimental data points were further used to verify the correlations, and ARD is only 9.50%, indicating that the acquired linear equations can provide reliable estimations. Additionally, the comparison between COSMO-RS and other models further illustrates that COSMO-RS is a reliable tool for predicting the heat capacity of ILs. Acknowledgements This work is financially supported by the Joint Research Fund for Overseas Chinese

13

Scholars and Scholars in Hong Kong and Macao Young Scholars (No. 21729601) and the National Natural Science Foundation of China (No. 21838004). YL and XJ thank the financial support from Carl Tryggers Stiftelse foundation (No. 18:175). XJ also thanks the financial support from Swedish Energy Agency (P50830-1).CL thanks the financial support from National Natural Science Foundation of China (No. 21878143). Supplementary Material (We have supplementary Material and attached them in the compressed file) References: [1] Y. Liu, Y. Wang, Y. Nie, C. Wang, X. Ji, L. Zhou, F. Pan, S. Zhang, Preparation of MWCNTs-graphene-cellulose fiber with ionic liquids, ACS Sustainable Chem. Eng. 7 (2019) 20013-20021. [2] F. Li, Y. Bai, S. Zeng, X. Liang, H. Wang, F. Huo, X. Zhang, Protic ionic liquids with low viscosity for efficient and reversible capture of carbon dioxide, Int. J. Greenh. Gas Control. 90 (2019) 102801-102801. [3] J. Li, Z. Dai, M. Usman, Z. Qi, L. Deng, CO2/H2 separation by amino-acid ionic liquids with polyethylene glycol as co-solvent, Int. J. Greenh. Gas Control. 45 (2016) 207-215. [4] J. Feng, H. Gao, L. Zheng, Z. Chen, S. Zeng, C. Jiang, H. Dong, L. Liu, S. Zhang, X. Zhang, A Mn-N3 single-atom catalyst embedded in graphitic carbon nitride for efficient CO2 electroreduction, Nat. Commun. 11 (2020) 4341-4341. [5] Y. Liu, K. Thomsen, Y. Nie, S. Zhang, A. Meyer, Predictive screening of ionic liquids for dissolving cellulose and experimental verification, Green Chem. 18 (2016) 6246-6254. [6] X. Liu, Y. Ren, L. Zhang, S. Zhang, Functional ionic liquid modified core-shell structured fibrous gel polymer electrolyte for safe and efficient fast charging lithium-ion batteries, Front. Chem. 7 (2019) 421-421. [7] I. Sujatha, G. Venkatarathnam, Performance of a vapour absorption heat transformer operating with ionic liquids and ammonia, Energy 141 (2017) 924-936. [8] Y. Zhao, Y. Huang, X. Zhang, S. Zhang, Prediction of heat capacity of ionic liquids based on COSMO-RS Sσ-profile, Computer Aided Chemical Engineering 37 (2015) 251-256. [9] Y. Xie, Y. Zhang, X. Lu, X. Ji, Energy consumption analysis for CO2 separation using imidazolium-based ionic liquids, Appl. Energy 136 (2014) 325-335.

14

[10] K. Müller, J. Albert, Contribution of the individual ions to the heat capacity of ionic liquids, Ind. Eng. Chem. Res. 53 (2014) 10343-10346. [11] K.G. Joback, A unified approach to physical property estimation using multivariant statistical techniques, M.S. Thesis, Massachusetts Institute of Technology Cambridge, America,1984. [12] R. Ge, C. Hardacre, J. Jacquemin, P. Nancarrow, D.W. Rooney, Heat capacities of ionic liquids as a function of temperature at 0.1 MPa. Measurement and prediction, J. Chem. Eng. Data 53 (2008) 2148–2153. [13] J. Jacquemin, J. Feder-Kubis, M. Zorębski, K. Grzybowska, M. ChorąŜewski, S. HenselBielówka, E. Zorębski, M. Paluch, M. Dzida, Structure and thermal properties of salicylatebased-protic ionic liquids as new heat storage media. COSMO-RS structure characterization and modeling of heat capacities, Phys. Chem. Chem. Phys. 16 (2014) 3549-3557. [14] M. Sattari, F. Gharagheizi, P. Ilani-Kashkouli, A.H. Mohammadi, D. Ramjugernath, Development of a group contribution method for the estimation of heat capacities of ionic liquids, J. Therm. Anal. Calorim. 115 (2013) 1863-1882. [15] A.N. Soriano, A.M. Agapito, L.J.L.I. Lagumbay, A.R. Caparanga, M.H. Li, A simple approach to predict molar heat capacity of ionic liquids using group-additivity method, J. Taiwan Inst. Chem. E. 41 (2010) 307-314. [16] X. Kang, X. Liu, J. Li, Y. Zhao, H. Zhang, Heat capacity prediction of ionic liquids based on quantum chemistry descriptors, Ind. Eng. Chem. Res. 57 (2018) 16989-16994. [17] A. Barati-Harooni, A. Najafi-Marghmaleki, M. Arabloo, A.H. Mohammadi, Chemical structural models for prediction of heat capacities of ionic liquids, J. Mol. Liq. 232 (2017) 113-122. [18] Y. Zhao, R. Gani, R.M. Afzal, X. Zhang, S. Zhang, Ionic liquids for absorption and separation of gases: An extensive database and a systematic screening method, AIChE J. 63 (2017) 1353-1367. [19] X. Liu, Y. Nie, Y. Liu, S. Zhang, A.L. Skov, Screening of ionic liquids for keratin dissolution by means of COSMO-RS and experimental verification, ACS Sustainable Chem. Eng. 6 (2018) 17314-17322. [20] J. Han, C. Dai, G. Yu, Z. Lei, Parameterization of COSMO-RS model for ionic liquids, Green Energy Environ. 3 (2018) 247-265. [21] X. Liu, T. Zhou, X. Zhang, S. Zhang, X. Liang, R. Gani, G.M. Kontogeorgis,

15

Application of COSMO-RS and UNIFAC for ionic liquids based gas separation, Chem. Eng.  Sci. 192 (2018) 816-828. [22] X. Zhang, Z. Liu, W. Wang, Screening of ionic liquids to capture CO2 by COSMO-RS and experiments, AIChE J. 54 (2008) 2717-2728. [23] Z.K. Koi, W.Z.N. Yahya, R.A. A. Talip, K.A. Kurnia, Prediction of the viscosity of imidazolium-based ionic liquids at different temperatures using the quantitative structure property relationship approach, New J. Chem. 43 (2019) 16207-16217. [24] J. Palomar, V.R. Ferro, J.S. Torrecilla, F. Rodrı´guez, Density and molar volume predictions using COSMO-RS for ionic liquids. An Approach to solvent design, Ind. Eng. Chem. Res. 46 (2007) 6041-6048. [25] Y. Liu, H. Yu, Y. Sun, S. Zeng, X. Zhang, Y. Nie, S. Zhang, X. Ji, Screening deep eutectic solvents for CO2 capture with COSMO-RS, Front. Chem. 8 (2020) 82-82. [26] I. Bandres, B. Giner, H. Artigas, F.M. Royo, C. Lafuente, Thermophysic comparative study of two isomeric pyridinium-based ionic liquids, J. Phys. Chem. B 112 (2008) 30773084. [27] C.M. Tenney, M. Massel, J.M. Mayes, M. Sen, J.F. Brennecke, E.J. Maginn, A computational and experimental study of the heat transfer properties of nine different ionic liquids, J. Chem. Eng. Data 59 (2014) 391-399. [28] A. Diedrichs, J. Gmehling, Measurement of heat capacities of ionic liquids by differential scanning calorimetry, Fluid Phase Equilibria 244 (2006) 68-77. [29] M. Kermanioryani, M.I.A. Mutalib, Y. Dong, K.C. Lethesh, O.B.O. Ben Ghanem, K.A. Kurnia, N.F. Aminuddin, J.-M. Leveque, Physicochemical properties of new imidazoliumbased ionic liquids containing aromatic group, J. Chem. Eng. Data 61 (2016) 2020-2026. [30] P.B.P. Serra, Thermal behavior and heat capacity of ionic liquids: benzilimidazolium and alkylimidazolium derivatives, M.S. Thesis, Universidade do Porto, Portugal, 2013. [31] J. Rotrekl, J. Storch, J. Kloužek, P. Vrbka, P. Husson, A. Andresová, M. Bendová, Z. Wagner,

Thermal

properties

of

1-alkyl-3-methylimidazolium

bis(trifluoromethylsulfonyl)imide ionic liquids with linear, branched and cyclic alkyl substituents, Fluid Phase Equilibria 443 (2017) 32-43. [32] Y.A. Sanmamed, P. Navia, D. Gonzalez-Salgado, J. Troncoso, L. Romani, Pressure and temperature dependence of isobaric heat capacity for [Emim][BF4], [Bmim][BF4], [Hmim][BF4], and [Omim][BF4], J. Chem. Eng. Data 55 (2010) 600-604.

16

[33] A.A. Strechan, Y.U. Paulechka, A.V. Blokhin, G.J. Kabo, Low-temperature heat capacity of hydrophilic ionic liquids [BMIM][CF3COO] and [BMIM][CH3COO] and a correlation scheme for estimation of heat capacity of ionic liquids, J. Chem. Thermodynamics 40 (2008) 632-639. [34] C.P. Fredlake, J.M. Crosthwaite, D.G. Hert, S.N.V.K. Aki, J.F. Brennecke, Thermophysical properties of imidazolium-based ionic liquids, J. Chem. Eng. Data 49 (2004) 954-964. [35] Y.U. Paulechka, A.G. Kabo, A.V. Blokhin, G.J. Kabo, M.P. Shevelyova, Heat capacity of ionic liquids: Experimental determination and correlations with molar volume, J. Chem. Eng. Data 55 (2010) 2719-2724. [36] M.M. Cruz, R.P. Borges, M. Godinho, C.S. Marques, E. Langa, A.P.C. Ribeiro, M.J.V. Lourenço, F.J.V. Santos, C.A. Nieto de Castro, M. Macatrão, M. Tariq, J.M.S.S. Esperança, J.N. Canongia Lopes, C.A.M. Afonso, L.P.N. Rebelo, Thermophysical and magnetic studies of two paramagnetic liquid salts: [C4mim][FeCl4] and [P66614][FeCl4], Fluid Phase Equilibria 350 (2013) 43-50. [37] Y.U. Paulechka, A.V. Blokhin, Low-temperature heat capacity and derived thermodynamic properties for 1-methyl-3-propylimidazolium bromide and 1-butyl-3methylimidazolium iodide, J. Chem. Thermodynamics 79 (2014) 94-99. [38] Y.-H. Yu, A.N. Soriano, M.-H. Li, Heat capacities and electrical conductivities of 1-nbutyl-3-methylimidazolium-based ionic liquids, Thermochim. Acta 482 (2009) 42-48. [39] A.A. Strechan, A.G. Kabo, Y.U. Paulechka, A.V. Blokhin, G.J. Kabo, A.S. Shaplov, E.I. Lozinskaya, Thermochemical properties of 1-butyl-3-methylimidazolium nitrate, Thermochim. Acta 474 (2008) 25-31. [40] J. Safarov, M. Geppert-Rybczynska, I. Kul, E. Hassel, Thermophysical properties of 1butyl-3-methylimidazolium acetate over a wide range of temperatures and pressures, Fluid Phase Equilibria 383 (2014) 144-155. [41] M.J. Davila, S. Aparicio, R. Alcalde, B. Garcia, J.M. Leal, On the properties of 1-butyl3-methylimidazolium octylsulfate ionic liquid, Green Chem. 9 (2007) 221-232. [42] S.N. Shah, K.C. Lethesh, M.I.A. Mutalib, R.B.M. Pilus, Evaluation of thermophysical properties of imidazolium-based phenolate ionic liquids, Ind. Eng. Chem. Res. 54 (2015) 3697-3705. [43] J. Troncoso, C.A. Cerdeirina, Y.A. Sanmamed, L. Romani, L.P.N. Rebelo,

17

Thermodynamic properties of imidazolium-based ionic liquids: Densities, heat capacities, and enthalpies of fusion of [bmim][PF6] and [bmim][NTf2], J. Chem. Eng. Data 51 (2006) 1856-1859. [44] A.A. Strechan, Y.U. Paulechka, A.G. Kabo, A.V. Blokhin, G.J. Kabo, 1-butyl-3methylimidazolium tosylate ionic liquid: Heat capacity, thermal stability, and phase equilibrium of its binary mixtures with water and caprolactam, J. Chem. Eng. Data 52 (2007) 1791-1799. [45] J. Safarov, F. Lesch, K. Suleymanli, A. Aliyev, A. Shahverdiyev, E. Hassel, I. Abdulagatov, Viscosity, density, heat capacity, speed of sound and other derived properties of 1-butyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate over a wide range of temperature and at atmospheric pressure, J. Chem. Eng. Data 62 (2017) 3620-3631. [46] J. Salgado, T. Teijeira, J. J. Parajo, J. Fernandez, J. Troncoso, Isobaric heat capacity of nanostructured liquids with potential use as lubricants, J. Chem. Thermodynamics 123 (2018) 107-116. [47] E. Zorębski, M. Musiał, K. Bałuszyńska, M. Zorębski, M. Dzida, Isobaric and isochoric heat capacities as well as isentropic and isothermal compressibilities of di- and trisubstituted imidazolium-based ionic liquids as a function of temperature, Ind. Eng. Chem. Res. 57 (2018) 5161-5172. [48] N. Calvar, E. Gomez, E.A. Macedo, A. Dominguez, Thermal analysis and heat capacities of pyridinium and imidazolium ionic liquids, Thermochim. Acta 565 (2013) 178-182. [49] Z.H. Zhang, L.X. Sun, Z.C. Tan, F. Xu, X.C. Lv, J.L. Zeng, Y. Sawada, Thermodynamic investigation of room temperature ionic liquid - Heat capacity and thermodynamic functions of BPBF4, J. Therm. Anal. Calorim. 89 (2007) 289-294. [50] E. Paulechka, A.V. Blokhin, A.S.M.C. Rodrigues, M.A.A. Rocha, L.M.N.B.F. Santos, Thermodynamics

of

long-chain

1-alkyl-3-methylimidazolium

bis(trifluoromethanesulfonyl)imide ionic liquids, J. Chem. Thermodynamics 97 (2016) 331340. [51] E. Gomez, N. Calvar, A. Dominguez, E.A. Macedo, Thermal analysis and heat capacities of 1-alkyl-3-methylimidazolium ionic liquids with NTf2-, TFO-, and DCA- anions, Ind. Eng. Chem. Res. 52 (2013) 2103-2110. [52] C. J. Rao, R. V. Krishnan, K.A. Venkatesan, K. Nagarajan, T.G. Srinivasan, Thermochemical properties of some bis(trifluoromethyl-sulfonyl)imide based room temperature ionic liquids, J. Therm. Anal. Calorim. 97 (2009) 937-943.

18

[53] Y.-H. Hsu, R.B. Leron, M.-H. Li, Solubility of carbon dioxide in aqueous mixtures of (reline+monoethanolamine) at T=(313.2 to 353.2) K, J. Chem. Thermodynamics 72 (2014) 94-99. [54] D. Waliszewski, I. Stepniak, H. Piekarski, A. Lewandowski, Heat capacities of ionic liquids and their heats of solution in molecular liquids, Thermochim. Acta 433 (2005) 149152. [55] I. Bandres, M. C. Lopez, M. Castro, J. Barbera, C. Lafuente, Thermophysical properties of 1-propylpyridinium tetrafluoroborate, J. Chem. Thermodynamics 44 (2012) 148-153. [56] Q.-S. Liu, Z.-C. Tan, U. Welz-Biermann, X.-X. Liu, Molar heat capacity and thermodynamic properties of N-alklypyridinium hexafluorophosphate salts, [Cnpy][PF6] (n=2, 3, 5), J. Chem. Thermodynamics 68 (2014) 82-89. [57] Y.-H. Yu, A.N. Soriano, M.-H. Li, Heat capacities and electrical conductivities of 1ethyl-3-methylimidazolium-based ionic liquids, J. Chem. Thermodynamics 41 (2009) 103108. [58] Z. Zhang, Z. Tan, L. Sun, J. Yang, X. Lv, Q. Shi, Thermodynamic investigation of room temperature ionic liquid: The heat capacity and standard enthalpy of formation of EMIES, Thermochim. Acta 447 (2006) 141-146. [59] C. Su, X. Liu, C. Zhu, M. He, Isobaric molar heat capacities of 1-ethyl-3methylimidazolium acetate and 1-hexyl-3-methylimidazolium acetate up to 16 MPa, Fluid Phase Equilibria 427 (2016) 187-193. [60] T. Makino, M. Kanakubo, Y. Masuda, H. Mukaiyama, Physical and CO2-absorption properties

of

imidazolium

ionic

liquids

with

tetracyanoborate

and

bis(trifluoromethanesulfonyl)amide anions, J. Solution Chem. 43 (2014) 1601-1613. [61] M. Krolikowska, K. Paduszynski, M. Krolikowski, P. Lipinski, J. Antonowicz, Vaporliquid phase equilibria and excess thermal properties of binary mixtures of ethylsulfate-based ionic liquids with water: New experimental data, correlations, and predictions, Ind. Eng. Chem. Res. 53 (2014) 18316-18325. [62] B. Tong, Q. Liu, Z. Tan, U. Welz-Biermann, Thermochemistry of alkyl pyridinium bromide ionic liquids: Calorimetric measurements and calculations, J. Phys. Chem. A 114 (2010) 3782-3787. [63] J. Benito, M. Garcia-Mardones, V. Perez-Gregorio, I. Gascon, C. Lafuente, Physicochemical study of n-ethylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquid,

19

J. Solution Chem. 43 (2014) 696-710. [64] M. Yang, J. Zhao, Q. Liu, L. Sun, P. Yan, Z. Tan, U. Welz-Biermann, Low-temperature heat capacities of 1-alkyl-3-methylimidazolium bis(oxalato)borate ionic liquids and the influence of anion structural characteristics on thermodynamic properties, Phys. Chem. Chem. Phys. 13 (2011) 199-206. [65] N.G. Polikhronidi, R.G. Batyrova, I.M. Abdulagatov, J.W. Magee, J. Wu, Thermodynamic properties at saturation derived from experimental two-phase isochoric heat capacity of 1-hexyl-3-methylimidazolium bis [(trifluoromethyl)sulfonyl] imide, Int. J. of Thermophys. 37 (2016) 103-138 [66] U. Domanska, R. Bogel-Lukasik, Physicochemical properties and solubility of alkyl-(2hydroxyethyl)-dimethylammonium bromide, J. Phys. Chem. B 109 (2005) 12124-12132. [67] N.M.C. Talavera-Prieto, A.G.M. Ferreira, P.N. Simoes, P.J. Carvalho, S. Mattedi, J.A.P. Coutinho,

Thermophysical

characterization

of

N-methyl-2-hydroxyethylammonium

carboxilate ionic liquids, J. Chem. Thermodynamics 68 (2014) 221-234. [68] R.L. Gardas, R. Ge, P. Goodrich, C. Hardacre, A. Hussain, D.W. Rooney, Thermophysical properties of amino acid-based ionic liquids, J. Chem. Eng. Data 55 (2010) 1505-1515. [69] N.G. Manin, A.V. Kustov, O.A. Antonova, Heat capacities of crystalline tetraalkylammonium salts, Russ. J. Phys. Chem. A 86 (2012) 878-880. [70] O. Yamamuro, T. Yamada, M. Kofu, M. Nakakoshi, M. Nagao, Hierarchical structure and dynamics of an ionic liquid 1-octyl-3-methylimidazolium chloride, J. Chem. Phys. 135 (2011) 054508-054508. [71] J. Safarov, C. Bussemer, A. Aliyev, C. Lafuente, E. Hassel, I. Abdulagatov, Effect of temperature on thermal (density), caloric (heat capacity), acoustic (speed of sound) and transport (viscosity) properties of 1-octyl-3-methylimidazolium hexafluorophosphate at atmospheric pressure, J. Chem. Thermodynamics 124 (2018) 49-64. [72] Y.U. Paulechka, A.V. Blokhin, G.J. Kabo, A.A. Strechan, Thermodynamic properties and

polymorphism

of

1-alkyl-3-methylimidazolium

bis(triflamides),

J.

Chem.

Thermodynamics 39 (2007) 866-877. [73] K. Oster, P. Goodrich, J. Jacquemin, C. Hardacre, A.P.C. Ribeiro, A. Elsinawi, A new insight into pure and water-saturated quaternary phosphonium-based carboxylate ionic liquids: Density, heat capacity, ionic conductivity, thermogravimetric analysis, thermal

20

conductivity and viscosity, J. Chem. Thermodynamics 121 (2018) 97-111. [74] A.F. Ferreira, P.N. Simoes, A.G.M. Ferreira, Quaternary phosphonium-based ionic liquids: Thermal stability and heat capacity of the liquid phase, J. Chem. Thermodynamics 45 (2012) 16-27.

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Declaration of interests

☒ The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper. ☐The authors declare the following financial interests/personal relationships which may be considered as potential competing interests:

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