Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm
Correction(s) for this article
-
Correction to “Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm”
- Volume 19Issue 6Asia-Pacific Journal of Chemical Engineering
- First Published online: November 4, 2024
Corresponding Author
Anantharaj Ramalingam
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Correspondence
Anantharaj Ramalingam, Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Rajiv Gandhi Salai (OMR), Kalavakkam, Tamilnadu 603110, India.
Email: [email protected]
Search for more papers by this authorTamal Banerjee
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Assam, India
Search for more papers by this authorVivek Mariappan Santhi
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorDhirendra Kumar Mishra
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Assam, India
Search for more papers by this authorDanish John Paul Mark Reji
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorShruthi Nagaraj
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorCorresponding Author
Anantharaj Ramalingam
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Correspondence
Anantharaj Ramalingam, Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Rajiv Gandhi Salai (OMR), Kalavakkam, Tamilnadu 603110, India.
Email: [email protected]
Search for more papers by this authorTamal Banerjee
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Assam, India
Search for more papers by this authorVivek Mariappan Santhi
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorDhirendra Kumar Mishra
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Assam, India
Search for more papers by this authorDanish John Paul Mark Reji
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorShruthi Nagaraj
Department of Chemical Engineering, Sri Sivasubramaniya College of Engineering, Tamilnadu, India
Search for more papers by this authorAbstract
In the present study, the potential of a selective green solvent for the low temperature esterification were analysed. Hence, 1-ethyl-3-methylimidazolium hydrogen sulphate {[EMIM][HSO4]},1-ethyl-3-methylimidazolium ethylsulphate {[EMIM][EtSO4]}, choline chloride glycerol {[ChCl][Gly]} and choline chloride acetic acid {[ChCl][AA]} were chosen as a selective green solvent. Whereas water, ethanol, acetic acid can be treated as molecular solvent used in the esterification process. In this reason, density of eight binary mixtures over the entire mole fractions were measured at different temperature ranges. The results have been used to calculate the excess and derived thermodynamic properties, to measure the strength of molecular interaction between mixing components. Further, the sigma profile and sigma potential plot were generated and analysed. According to density, volumetric properties, molecular polarity results, 1-ethyl-3-methylimidazolium hydrogen sulphate [EMIM][HSO4] was chosen as green solvent for the green esterification process. Finally, [EMIM][HSO4] based low temperature esterification were conducted at 298.15 K and 1 atm. 80.96% of n-BuAc was achieved.
Supporting Information
Filename | Description |
---|---|
apj2875-sup-0001-Supporting Material for Review and Publication.docxWord 2007 document , 4.7 MB |
Table S1: The density correlation parameters a, b, c and σ for all the studied systems. Table S2: All the Binary system used in this study, molecular formula, Miscibility, Hetero atoms. Functional groups and its numbers. Table S3: Chemical structure and sigma surface with possible specific and/or non-specific interactions during mixing at molecular level. Table S4: Excess molar volume of ethanol (1) +acetic acid (2), Ethanol (1) + [EMIM][HSO4] (2), Ethanol (1) + DES-1(AA), Ethanol (1) + DES-2(Gly) and Ethyl Acetate (1) + Acetic Acid (2) over the entire mole fractions and at different temperatures. Table S5: The partial molar volume (cm3/mol),excess partial molar volume (cm3/mol) and apparent molar volume (cm3/mol) of individual compounds at different temperatures and 1 atm. Table S6: Isobaric expansivity for the studied binary mixtures over the whole composition range from temperature 293.15 K to 343.15 K and atmospheric pressure. Table S7: Excess Isobaric expansivity for the studied binary mixtures over the whole composition range from temperature 293.15 K to 343.15 K and atmospheric pressure. Table S8. Comparison of sigma profile of all the studied chemical species by MATLAB Code, COSMOThermX and Free Tool (COSMO-SAC). Table S9: Reaction feed specification that has been carried out in thhis work at 298.15 K and 1 atm. Figure S1: Experimental densities of Ethanol + Acetic Acid as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S2: Experimental densities of Ethanol + n- Ethyl Acetate as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S3: Experimental densities of Ethanol + Water as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S4: Experimental densities of Ethanol + [EMIM][HSO4] as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S5: Experimental densities of Ethanol + [EMIM][EtSO4] as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S6: Experimental densities of Ethanol + [ChCl][AA] as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S7: Experimental densities of Ethanol + [ChCl][Gly] as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S8: Experimental densities of Ethyl Acetate + Acetic Acid as a function of temperature. The line corresponds to the fit of the data by Equation 1 reported in Table 1. Figure S9: Sigma profile of organic solvents. Figure S10: Sigma profile of ionic liquids and deep eutectic solvents. Figure S11: Sigma profile of ethyl acetate, ionic liquids and deep eutectic solvents. Figure S12: Sigma Profile of [HAc]. Figure S13: Sigma Profile of [EtAc]. Figure S14: Sigma Profile of [EtOH]. Figure S15: Sigma Profile of [EMIM]. Figure S16: Sigma Profile of [EtSO4]. Figure S17: Sigma Profile of [HSO4]. Figure S18: Sigma Profile of [EMIM][EtSO4]. Figure S19: Sigma Profile of [EMIM][HSO4]. Figure S20: Sigma Profile of [ChCl]. Figure S21: Sigma Profile of [Gly]. Figure S22: Sigma Profile of [ChCl][HAc]. Figure S23: Sigma Profile of [ChCl][Gly]. Figure S24: Sigma potential of organic solvents. Figure S25: Sigma potential of ionic liquids and deep eutectic solvents. Figure S26: Sigma potential of ethyl sulphate, Ionic Liquids and deep eutectic solvents. Figure S27: FTIR spectra of pure n-EtAc. Figure S28: FTIR spectra of n-EtAc using [EMIM][HSO4] at 7:3 ratio. Figure S29: FTIR spectra of n-EtAc using [EMIM][HSO4] at 7:4 ratio. Figure S30: U V Spectra of pure ethyl acetate. Figure S31: UV Spectra of synthesized ethyl acetate using [EMIM][HSO4] at 7:3 reactant Ratio. Figure S32: UV Spectra of synthesized ethyl acetate using [EMIM][HSO4] at 7:4 reactant ratio. Figure S33: GC-FID spectra of pure ethyl acetate. Figure S34: GC-FID spectra of synthesized ethyl acetate using [EMIM][HSO4] at 7:3 reactant ratio. Figure S35: GC-FID spectra of synthesized ethyl acetate using [EMIM][HSO4] at 7:4 reactant ratio |
Please note: The publisher is not responsible for the content or functionality of any supporting information supplied by the authors. Any queries (other than missing content) should be directed to the corresponding author for the article.
REFERENCES
- 1Lin T-B, Chung D-L, Chang J-R. Ethyl acetate production from water-containing ethanol catalyzed by supported Pd catalysts: advantages and disadvantages of hydrophobic supports. Ind Eng Chem Res. 1999; 38(4): 1271-1276. doi:10.1021/ie9805887
- 2Hanika J, Kucharova M, Kolena J, Smejkal Q. Multi-functional trickle bed reactor for butyl acetate synthesis. Catal Today. 2003; 79-80: 83-87. doi:10.1016/S0920-5861(03)00013-0
- 3Jyoti G, Amit Keshav J, Kumar A. Experimental and kinetic study of esterification of acrylic acid with ethanol using homogeneous catalyst. Int J Chem React Eng. 2016; 14(2): 571-578. doi:10.1515/ijcre-2015-0131
- 4Beula C, Sai PST. Enhancement of esterification reaction using ionic liquid as catalyst with simultaneous removal of water. Int J Chem Eng Appl. 2013; 3: 388-392. doi:10.7763/IJCEA.2013.V4.331
10.7763/IJCEA.2013.V4.331 Google Scholar
- 5Mallakpour S, Dinari M. Ionic liquids as green solvents: Progress and prospects. Green Solvents. 2012; 1-32. doi:10.1007/978-94-007-2891-2_1
10.1007/978?94?007?2891?2_1 Google Scholar
- 6Reddy MS, Raju KTSS, Nayeem SM, Khan I, Krishana KBM, Babu BH. Excess thermodynamic properties for binary mixtures of ionic liquid 1-Ethyl-3-methylimidazolium ethyl sulfate and 2-Methoxyethanol from T 5 (298.15 to 328.15) K at atmospheric pressure. J Solution Chem. 2016; 45(5): 675-701. doi:10.1007/s10953-016-0465-y
- 7Oliveira FS, Pereiro AB, Rebelo LPN, Marrucho IM. Deep eutectic solvents as extraction media for azeotropic mixtures. Green Chem. 2013; 15(5): 1326. doi:10.1039/c3gc37030e
- 8Sas OG, Fidalgo R, Domínguez I, Macedo EA, González B. Physical properties of the pure deep eutectic solvent, [ChCl]:[lev](1:2) DES, and its binary mixtures with alcohols. J Chem Eng Data. 2016; 6112: 4191-4202.
- 9Smith E, Abbott AP, Ryder KS. Deep eutectic solvents (DESs) and their applications. ChemRev. 2014; 114(21): 11060-11082. doi:10.1021/cr300162p
- 10Yadav A, Trivedi S, Rai R, Pandey S. Densities and dynamic viscosities of (choline chloride + glycerol) deep eutectic solvent and its aqueous mixtures in the temperature range (283.15–363.15) K. Fluid Phase Equ. 2014; 367: 135-142. doi:10.1016/j.fluid.2014.01.028
- 11Ju-Hwan O, Lee J-S. Synthesis of gold microstructures with surface Nanoroughness using a deep eutectic solvent for catalytic and diagnostic applications. J Nano Sci Nanotech. 2014; 14(5): 3753-3757. doi:10.1166/jnn.2014.8658
- 12Jia T, Bi S, Wu J. Compressed liquid densities of binary mixtures of ndecane+ n-dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa. Fluid Phase Equilibria. 2018; 459: 65-72. doi:10.1016/j.fluid.2017.12.010
- 13Rajendran Startha Christabel A, Ramalingam A, Reji DJPM, Nagaraj S, Ravichandran S. Liquid densities and excess quantities for the green esterification process. Chemical & Engineering Data Series. 65(2): 446-476. doi:10.1021/acs.jced.9b00453
10.1021/acs.jced.9b00453 Google Scholar
- 14Man MS, Abdullah MAM, Abdullah SB, Yaacob Z. Screening cation and anion of ionic liquid for dissolution of silicon dioxide using COSMO-RS. Ind J Sci Tech. 2017; 10(6): 1-6. doi:10.17485/ijst/2017/v10i6/111218
- 15Pereiro AB, Rodrıguez A. Thermodynamic properties of ionic liquids in organic solvents from (293.15 to 303.15) K. J Chem Eng Data. 2007; 52(2): 600-608. doi:10.1021/je060497d
- 16Zhong Y, Wang H, Diao K. Densities and excess volumes of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate with aromatic compound at T = (298.15 to 313.15) K. J Chem Therm. 2007; 39(2): 291-296. doi:10.1016/j.jct.2006.07.001
- 17Singh T, Kumar A. Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K. J Chem Therm. 2008; 40(3): 417-423. doi:10.1016/j.jct.2007.09.011
- 18Pereiro AB, Rodrı´guez A. Measurement and correlation of (liquid + liquid) equilibrium of the azeotrope (cyclohexane + 2-butanone) with different ionic liquids at T = 298.15 K. J Chem Therm. 2008; 40(8): 1282-1289. doi:10.1016/j.jct.2008.03.011
- 19Gao H, Qi F, Wang H. Densities and volumetric properties of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate with benzaldehyde at T = (298.15 to 313.15) K. J Chem Therm. 2009; 41(7): 888-892. doi:10.1016/j.jct.2009.02.007
- 20Bhuiyan MMH, Uddin MH. Excess molar volumes and excess viscosities for mixtures of N,N-dimethylformamide with methanol, ethanol and 2-propanol at different temperature. J Mol Liq. 2008; 138(1-3): 139-146. doi:10.1016/j.molliq.2007.07.006
- 21Wisniak J, Cortez G, Peralta RD, Infante R, Elizalde LE. Some thermodynamic properties of the binary Systems of Toluene with butyl methacrylate, allyl methacrylate, Methacrylic acid and vinyl acetate at 20, 30 and 40 °C. J sol Chem. 2007; 36(8): 997-1022. doi:10.1007/s10953-007-9165-y
- 22Anantharaj R, Banerjee T. Thermodynamic properties of 1-ETHYL-3-methylimidazolium methanesulphonate with aromatic Sulphur, nitrogen compounds atT = 298.15-323.15 K and P = 1 bar. J Chem Eng. 2012; 91(2): 245-256. doi:10.1002/cjce.21638
- 23Kumari A, Sandeepa K, Prathap Kumar T, Satyavathi B. Solubility, thermodynamic properties, and derived excess properties of benzoic acid in (acetic acid + water) and (acetic acid + toluene) binary mixtures. J. Chem. Eng. 2016; 61(1): 67-77. doi:10.1021/acs.jced.5b00197
- 24Domanska U, Królikowska M, Królikowski M. Phase behaviour and physico-chemical properties of the binary systems {1-ethyl-3-methylimidazolium thiocyanate, or 1-ethyl-3-methylimidazolium tosylate + water, or + an alcohol}. Fluid Phase Equilibria. 2010; 294(1-2): 72-83. doi:10.1016/j.fluid.2010.01.020
- 25Gonzalez B, Domınguez I, Gonzalez EJ, Domınguez A. Density, speed of sound, and refractive index of the binary systems cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with benzene (2), toluene (2), and ethylbenzene (2) at two temperatures. J Chem Eng Data. 2010; 55(2): 1003-1011. doi:10.1021/je900468u
- 26Anouti M, Caillon-Caravanier M, Dridi Y, Jacquemin J, Hardacre C, Lemordant D. Liquid densities, heat capacities, refractive index and excess quantities for {protic ionic liquids + water} binary system. J Chem Therm. 2009; 41(6): 799-808. doi:10.1016/j.jct.2009.01.011
- 27Wang S, Jacquemin J, Husson P, Hardacre C, Costa MF, Gomes. Liquid–liquid miscibility and volumetric properties of aqueous solutions of ionic liquids as a function of temperature. J Chem Therm. 2009; 41(11): 1206-1214. doi:10.1016/j.jct.2009.05.009
- 28García-Miaja G, Troncoso J, Romaní L. Excess enthalpy, density, and heat capacity for binary systems of alkylimidazolium-based ionic liquids + water. J Chem Therm. 2009; 41(2): 161-166. doi:10.1016/j.jct.2008.10.002
- 29Yang C, Ma P, Zhou Q. Excess molar volume, viscosity, and heat capacity for the mixtures of 1,4-Butanediol + water at different temperatures. J Chem Eng Data. 2004; 49(3): 582-587. doi:10.1021/je0341918
- 30Gonzalez EJ, Luisa Alonso A, Domınguez Ä. Physical properties of binary mixtures of the ionic liquid 1-methyl-3-octylimidazolium chloride with methanol, ethanol, and 1-propanol at T=(298.15, 313.15, and 328.15) K and at P= 0.1 MPa. J Chem Eng Data. 2006; 51(4): 1446-1452. doi:10.1021/je060123k
- 31Gómez E, González B, Calvar N, Tojo E, Domínguez Á. Physical properties of pure 1-Ethyl-3-methylimidazolium Ethylsulfate and its binary mixtures with ethanol and water at several temperatures. J Chem Eng Data. 2006; 51(6): 2096-2102. doi:10.1021/je060228n
- 32Rodrıguez H, Brennecke JF. Temperature and composition dependence of the density and viscosity of binary mixtures of water + ionic liquid. J Chem Eng Data. 2006; 51(6): 2145-2155. doi:10.1021/je0602824
- 33Zarei HA. Densities, excess molar volumes and partial molar volumes of the binary mixtures of acetic acid+alkanol (C1–C4) at 298.15 K. J Mol Liq. 2007; 130(1-3): 74-78. doi:10.1016/j.molliq.2006.04.009
- 34Chen H-W, Wen C-C, Chein-Hsiun T. Excess molar volumes, viscosities, and refractive indexes for binary mixtures of 1-Chlorobutane with four alcohols at T=(288.15, 298.15, and 308.15) K. J Chem Eng Data. 2004; 49(2): 347-351. doi:10.1021/je030226s
- 35Reichardt C. Polarity of ionic liquids determined empirically by means of solvatochromic pyridinium N-phenolate betaine dyes. Green Chem. 2005; 7(5): 339-351. doi:10.1039/b500106b
- 36Sitze MS, Schreiter ER, Patterson EV, Griffith Freeman R. Ionic liquids based on FeCl3 and FeCl2. Raman scattering and ab initio calculations. Inorg Chem. 2001; 40(10): 2298-2304. doi:10.1021/ic001042r
- 37Suezawa H, Hashimoto T, Tsuchinaga K, et al. Electronic substituent effect on intramolecular CH/π interaction as evidenced by NOE experiments. J Chem Soc Perkin Trans. 2000; 2(6): 1243-1249. doi:10.1039/a909450d
10.1039/a909450d Google Scholar
- 38Liu W-X, Jiang Y-B. Intramolecular hydrogen bonding and anion binding of N-Benzamido-N-benzoylthioureas. J Org Chem. 2008; 73(3): 1124-1127. doi:10.1021/jo702159r
- 39Acharya P, Plashkevych O, Morita C, Yamada S, Chattopadhyaya J. A repertoire of Pyridinium-phenyl-methyl cross-talk through a Cascade of intramolecular electrostatic interactions. J Org Chem. 2003; 68(4): 1529-1538. doi:10.1021/jo026572e
- 40Lassègues J-C, Grondin J, Cavagnat D, Johansson P. New interpretation of the CH stretching vibrations in imidazolium-based ionic liquids. J Phys Chem a. 2009; 113(23): 6419-6421. doi:10.1021/jp903160r
- 41Zhang S, Qi X, Ma X, Liujin L, Deng Y. Hydroxyl ionic liquids: the differentiating effect of hydroxyl on polarity due to ionic hydrogen bonds between hydroxyl and anions. J Phys Chem B. 2010; 114(11): 3912-3920. doi:10.1021/jp911430t
- 42Zhang Q-G, Wang N-N, Zhi-Wu Y. The hydrogen bonding interactions between the ionic liquid 1-Ethyl-3-Methylimidazolium ethyl sulfate and water. J Phys Chem B. 2010; 114(14): 4747-4754. doi:10.1021/jp1009498
- 43Fernandes AM, Rocha MAA, Freire MG, Marrucho IM, Coutinho JAP, Santos LMNBF. Evaluation of CationAnion interaction strength in ionic liquids. J Phys Chem B. 2011; 115(14): 4033-4041. doi:10.1021/jp201084x
- 44Izgorodina EI, MacFarlane DR. Nature of hydrogen bonding in charged hydrogen-bonded complexes and imidazolium-based ionic liquids. J Phys Chem B. 2011; 115(49): 14659-14667. doi:10.1021/jp208150b
- 45Dong K, Song Y, Liu X, Cheng W, Yao X, Zhang S. Understanding structures and hydrogen bonds of ionic liquids at the electronic level. J Phys Chem B. 2012; 116(3): 1007-1017. doi:10.1021/jp205435u
- 46Skarmoutsos I, Dellis D, Matthews RP, Welton T, Hunt PA. Hydrogen bonding in 1-butyl- and 1-Ethyl-3-methylimidazolium chloride ionic liquids. J Phys Chem B. 2012; 116(16): 4921-4933. doi:10.1021/jp209485y
- 47González B, Domínguez A, Tojo J. Dynamic viscosities, densities, and speed of sound and derived properties of the binary systems acetic acid with water, methanol, ethanol, ethyl acetate and methyl acetate atT= (293.15, 298.15, and 303.15) K at atmospheric pressure. J Chem Eng Data. 2004; 49(6): 1590-1596. doi:10.1021/je0342825
- 48Gonzalez B, Calvar N, Gomez E, Domınguez A. Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K. J Chem Thermodyn. 2007; 39(12): 1578-1588. doi:10.1016/j.jct.2007.05.004
- 49Nikumbh A, Kulkarni G. Density and viscosity study of binary mixtures of ethanol -water at different temperatures. Sci J Pure Appl Chem. 2013; 196(13). doi:10.7237/sjpac/196
10.7237/sjpac/196 Google Scholar
- 50Redlich O, Kister AT. Thermodynamics of nonelectrolyte solutions. Algebraic representation of thermodynamic properties and the classification of solutions. Ind Eng Chem. 1948; 40(2): 345-348. doi:10.1021/ie50458a036
- 51Chenga H, Liua C, Zhanga J, Chena L, Zhangb B, Qia Z. Screening deep eutectic solvents for extractive desulfurization of fuel based on COSMO-RS model. Chem Eng Process: Process Inten. 2018; 125: 246-252. doi:10.1016/j.cep.2018.02.006
- 52Klamt A, Eckert F. COSMO-RS: a novel and efficient method for the a priori prediction of thermophysical data of liquids. Fluid Phase Equilibria. 2000; 172(1): 43-72. doi:10.1016/S0378-3812(00)00357-5
- 53Tiancheng M. Group contribution prediction of surface charge density profiles for COSMO-RS (Ol). AIChE Journal. 2007; 53(12): 3231-3240. doi:10.1002/aic.11338
- 54Naydenov D, Bart H-J. Ternary liquid−liquid equilibria for six systems containing Ethylacetate + ethanol or acetic acid + an imidazolium-based ionic liquid with a hydrogen sulfate anion at 313.2 K. J Chem Eng Data. 2007; 52(6): 2375-2381. doi:10.1021/je700342k
- 55Naydenov D, Bart H-J. Ternary liquid−liquid equilibria for systems containing alcohol or acetic acid + Ester + 1-Ethyl-3-methylimidazolium hydrogen sulfate at 313.2 K using headspace gas chromatography. J Chem Eng Data. 2009; 54(1): 43-47. doi:10.1021/je800547k
- 56Bell IH, Mickoleit E, Hsieh C-M, et al. A benchmark open-source implementation of COSMO-SAC. J Chem Theory Comput. 2020; 16(4): 2635-2646. doi:10.1021/acs.jctc.9b01016
- 57Xiong R, Sandler SI, Burnet RI. An improvement to COSMO-SAC for predicting thermodynamic properties. Ind Eng Chem Res. 2014; 53(19): 8265-8278. doi:10.1021/ie404410v
- 58Islam MR, Chen C-C. COSMO-SAC sigma profile generation with conceptual segment concept. Ind Eng Chem Res. 2015; 54(16): 4441-4454. doi:10.1021/ie503829b
- 59Leron RB, Wong DSH, Li MH. Densities of a deep eutectic solvent based on choline chloride and glycerol and its aqueous mixtures at elevated pressures. Fluid Phase Equilibria. 2012; 335: 32-38. doi:10.1016/j.fluid.2012.08.016