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Article

Abraham Solvation Parameter Model: Calculation of L Solute Descriptors for Large C11 to C42 Methylated Alkanes from Measured Gas–Liquid Chromatographic Retention Data

Department of Chemistry, University of North Texas, Denton, TX 76203, USA
*
Author to whom correspondence should be addressed.
Liquids 2022, 2(3), 85-105; https://doi.org/10.3390/liquids2030007
Submission received: 16 June 2022 / Revised: 30 June 2022 / Accepted: 1 July 2022 / Published: 5 July 2022
(This article belongs to the Collection Feature Papers in Solutions and Liquid Mixtures Research)

Abstract

:
Abraham model L solute descriptors have been determined for 149 additional C11 to C42 monomethylated and polymethylated alkanes based on published Kovat’s retention indices based upon gas–liquid chromatographic measurements. The calculated solute descriptors, in combination with previously published Abraham model correlations, can be used to predict a number of very important chemical and thermodynamic properties including partition coefficients, molar solubility ratios, gas–liquid chromatographic and HPLC retention data, infinite dilution activity coefficients, molar enthalpies of solvation, standard molar vaporization and sublimation at 298 K, vapor pressures, and limiting diffusion coefficients. The predictive computations are illustrated by estimating both the standard molar enthalpies of sublimation and the enthalpies of solvation in benzene for the monomethylated and polymethylated alkanes considered in the current study.

1. Introduction

Scientists and engineers in both academia and the industrial manufacturing sector must rely upon empirical and semi-theoretical models to predict the thermodynamic and physical properties required in process design calculations. Even with today’s modern instrumentation it is not feasible to experimentally determine the properties for the more than 60 million known chemical compounds [1]. Chemical manufacturing processes rarely contain only a single compound. Experimental measurements become even more challenging when one takes into account the number of possible binary, ternary and higher-order multicomponent mixtures that can be prepared from existing compounds. The number of possible combinations increases annually as new compounds are synthesized, found and identified.
Over the last 50 years numerous predictive methods have been developed based upon either quantitative structure–property relationships (QSPRs) or group contribution concepts. QSPR methods [2,3,4,5,6,7,8] identify mathematical relationships between the desired property that one wishes to calculate and other physical properties or from compound descriptor values that can be derived from molecular structure and/or quantum mechanical considerations. For some published QSPR studies [2,6,8] more than 1000 different descriptors have been considered before narrowing the descriptor set down to those yielding the desired predictive accuracy. Group contribution methods [9,10,11,12,13,14,15,16], on the other hand, fragment the given molecule into atoms or functional groups. A numerical value is then assigned to each atom or fragment group. In the simplest case the desired property would be calculated as the summation of the product of the number of occurrences each fragment group appears in the molecule times its respective numerical group value. Naturally the method would be limited to those molecules having known functional group values.
The predictive method that we have been using to predict thermodynamic and physical properties is based upon the Abraham solvation parameter model [17,18,19,20] which defines solute transfer between two immiscible (or partly miscible) phases in terms of a linear free energy relationship (LFER). The first LFER:
Solute Property = e1 × E + s1 × S + a1 × A + b1 × B + v1 × V + c1
describes solute transfer between two condensed phases, while the second LFER:
Solute Property = e2 × E + s2 × S + a2 × A + b2 × B + l2 × L + c2
describes solute transfer into a condensed phase from the gas phase. Specific properties that have been successfully described include partition coefficients [20,21,22], molar solubility ratios [19,23,24], aquatic toxicities [25,26,27], nasal pungencies [28], gas–liquid chromatographic and HPLC retention data [18,29,30,31,32,33], Draize scores and eye irritation thresholds [34,35], human and rat intestinal adsorption data [36,37], human skin permeability [38,39], infinite dilution activity coefficients [40,41], molar enthalpies of solvation [42,43,44], standard molar vaporization [45] and sublimation [46] at 298 K, vapor pressures [47], and limiting diffusion coefficients [48,49].
Unlike many of the QSPRs that have been proposed in the published chemical and engineering literature, Equations (1) and (2) are based upon a fundamental understanding of how molecules interact in solution. The first five terms on the right-hand side of both Equations (1) and (2) represent a different type of molecular interaction that is described by the product of a solute property (E, S, A, B, V and L) times its complimentary solvent or process property (e1, s1, a1, b1, v1, c1, e2, s2, a2, b2, l2 and c2). The uppercase alphabetical characters in both Abraham model correlations are called solute descriptors, and are defined in the following manner: A and B represent the respective overall hydrogen-bond donating and accepting abilities of the dissolved solute; E denotes the given solute’s excess molar refraction referenced to that of a linear alkane having a comparable molecular size; L refers to the logarithm of the solute’s gas-to-hexadecane partition coefficient determined at 298.15 K; S corresponds to a combination of the electrostatic polarity and polarizability of the solute; and V is the solute’s McGowan molecular volume calculated from known sizes of the constituent atoms and chemical bond numbers. The numerical values of the lowercase solvent or process property are determined by a least-squares analysis that involves curve-fitting the measured property for a series of solutes with known descriptor values in a given solvent (or for a given process) in accordance with Equations (1) and (2) of the Abraham model. The calculated numerical values of solvent/process equation coefficients depend upon the organic solvent or process under consideration. In other words, the equation coefficients that describe the enthalpy of solvation of organic solutes dissolved in benzene are numerically different than the values that describe the enthalpy of solvation of organic solutes in dimethyl sulfoxide. The Abraham model is described in greater detail elsewhere [17,18,50,51,52].
One major advantage that the Abraham model offers over most predictive QSPRs is that the same numerical values of the solute descriptors are used in every Abraham model correlation, irrespective of the chemical property being predicted. This feature avoids having to calculate a new set of solute descriptors every time that one wishes to predict a different chemical property. A common set of solute descriptors for every correlation also permits one to directly compare the solubilizing properties of different organic solvents and two-phase partitioning systems through Principal Component Analysis, the Euclidean distance formula and other computational methods. Such comparisons might be used to assist design engineers in identifying less toxic, more environmentally compatible solvent alternatives to replace the more hazardous organic solvents currently used in industrial manufacturing processes, or to help in identifying partition systems that might mimic biological response properties. These latter comparisons have involved skin permeation and water-to-organic solvent systems [38], parallel artificial membrane permeability assays and biological systems [53], and aquatic toxicity and water-to-organic solvent systems [25,27]. Each of the fore-mentioned comparisons described both the specified biological and chemical process in terms of an Abraham model correlation.
At present, experimental-based solute descriptors are available for more than 8500 different molecular organic and organometallic compounds and for more than 300 different ionic species (such as tetraalkylammonium and substituted-pyridinium cations, substituted-phenolate and substituted-benzoate anions), which is only a tiny fraction of the known chemical compounds. Recognizing that it will never be possible to perform a sufficient number of experimental measurements to calculate experimental-based Abraham model solute descriptors for every known chemical compound, researchers have searched for alternative methods to estimate the numerical values. Published group contribution [53,54,55,56] and machine learning methods [55,56] have exhibited remarkable promise in that both the molar enthalpies of solvation (ΔHsolv) and molar Gibbs energies of solvation (ΔGsolv) of molecular organic solutes and inorganic gases in a wide range of organic solvents of varying polarity and hydrogen-bonding character could be reasonably predicted by the estimated solute descriptors. In the study by Chung and coworkers [56] the authors used an “inhouse” solute descriptor database containing 8366 unique chemical compounds. The compounds were fragmented into atom-centered (AC) functional groups. Each solute descriptor was then calculated by:
E ,   S ,   A ,   B   or   L = i = 1 N a t o m A C i +   j = 1   R S C j + k = 1   L D I k
summing the contributions from all AC groups, with special ring strain corrections (RSC) and long-distance interaction (LDI) groups being added to account for any more advanced structural features that were not fully captured by the atom-centered approach. Halogenated molecules required a slightly different estimation scheme in that the halogenated atoms were replaced by hydrogen atoms prior to the fragmentation. The correction(s) for the halogen atom(s) were added at the end to the calculated solute descriptor of the “non-halogenated compound”:
E ,   S ,   A ,   B   or   L = i = 1 N a t o m * A C i +   j = 1   R S C j + k = 1   L D I k +   l = 1 N h a l o g e n H a l o g e n l
where Natom* and Nhalogen denote the number of non-halogen heavy atoms and the number of halogen atoms in the given molecule, respectively. The numerical values of the individual AC groups, as well as all RSC, LDI and Halogen values, were determined by regressing the known descriptor values in accordance with Equations (3) and (4). The authors developed a machine learning method for estimating solute descriptors. Both predictive methods are very easy to use as the authors provided a link to the computational software. Users simply enter the canonical SMILES code of the molecule into the software. The results of the authors’ calculations showed that solute descriptors estimated by the machine learning method provided the better test set predictive values for both ΔHsolv and ΔGsolv with mean absolute errors of MAE = 3.89 kJ/mole and MAE = 4.184 kJ/mole, respectively. Slightly larger test set errors of MAE = 4.73 kJ/mole (ΔHsolv) and MAE = 4.94 kJ/mole (ΔGsolv) were noted in the case of the solute descriptors estimated by the authors’ group contribution method. The study by Ulrich and Ebert [57] used the slightly smaller Abraham Absolv solute parameter database found on the UFZ-LSER internet website [58] in developing their group contribution and deep machine learning methods for estimating solute descriptors. Methods aimed at predicting the Abraham model process coefficients have had mixed success; in part, because experimental-based correlations have been developed for relatively few organic solvents and biphasic partition systems [59,60,61,62].
The continued development of predictive group contribution and machine learning methods for the Abraham model requires the determination of both experimental-based solute descriptors and experimental-based solvent/process correlations. Additional experimental measurements are also needed for testing the limitations and applications of new predictive methods. To aid in future endeavors, we have recently reported solute descriptors for an additional 174 monomethyl branched alkanes [63], for an additional 127 C9–C26 mono-alkyl alkanes and polymethyl alkanes [64], for an additional 33 linear C7–C14 alkynes [65], and for several important active pharmaceutical ingredients and intermediates [23,66,67,68]. Abraham model correlations have also been recently determined for two practical partitioning systems, water-methyl ethyl ketone (MEK) [21] and water-methyl isobutyl ketone (MIBK) [22], and for solute transfer into isopropyl acetate [69], anisole [70] and cyclohexanol [71]. In the current communication we have calculated Abraham model L solute descriptor values for an additional 149 C11 to C44 methylated alkanes from measured gas–liquid chromatographic retention data gathered from a compilation by Katritzky and coworkers [72].

2. Calculation of Abraham Model Solute Descriptors for Methylated Alkanes

Normally the determination of Abraham model solute descriptors involves constructing a series of mathematical expressions for the measured solute properties of the given solute in a series of solvents and/or for a series of processes for which the lowercase equation coefficients are known. The solute properties used in past descriptor calculations have included logarithms of the measured solubility ratio of the solute in several different organic mono-solvents, the logarithms of the measured water-to-organic solvent partition coefficients, measured gas–liquid chromatographic retention data, and/or experimental enthalpies of solvation for the solute dissolved in several different organic solvents. Each of these solute properties will hopefully have very little experimental error. Aquatic toxicities and biological response factors generally have too much experimental error to be used effectively in solute descriptor calculations.
The Abraham model expressions for each of the fore-mentioned processes contain a common set of solute descriptors. The series of mathematical expressions are then solved for the “best” set of descriptor values that minimizes the overall squared-summed difference between the measured properties and the respective back-calculated values based on Equations (1) and (2). For the methylated hydrocarbons listed in Table 1, the computational process is greatly simplified in that the E, S, A and B solute descriptors are all equal to zero. The V solute descriptor is readily calculated from the solute’s molecular structure, the atomic volumes of the constituent atoms contained in the solute molecule, and the number of chemical bonds in the solute molecule as described by Abraham and McGowan [73]. This leaves only the L solute descriptor to be calculated.
To calculate the L solute descriptor based on the gas–liquid chromatographic data retrieved from the published paper by Katritzky and coworkers [72], we first must establish a mathematical relationship correlation between the reported Kovat’s retention indices, KRI, and the L solute descriptor for alkane solute molecules. Numerical values KRI are available for 178 methylated alkanes [73]; however, for most of the molecules the L solute descriptor is not known. We can increase the number of compounds used in establishing the Abraham model correlation by noting that by definition the KRI values of linear alkanes is simply 100 times the number of carbon atoms. This allows us to add an additional 34 alkanes (heptane through tetracontane) to the regression data set. By combining the 34 linear alkanes and the 29 monomethyl alkanes with known L descriptor values from the Katritzky et al. compilation [72], we have 63 experimental data points to use in developing our Abraham model KRI versus L descriptor correlation.
Analysis of the values in the second and third columns of Table 1 yielded the following Abraham model expression:
L = 0.504 (0.001) × (KRI/100) − 0.356 (0.012)
(N = 63, SD = 0.034, R2 = 1.000 and F = 942,023)
where N is the number of experimental data points used in the linear least-squares analysis, SD is the standard deviation, R2 is the squared correlation coefficient, and F is the Fisher F-statistic. Standard errors in the slope and intercept are given in parentheses immediately following the respective equation coefficient. Equation (5) back-calculates the L values used in the least-squares analysis to within an average absolute deviation of AAE = 0.025 and an average error of AE = −0.006. Figure 1 depicts the linear plot of the L descriptor values versus KRI/100 values for the 63 data points used in deriving Equation (5). The derived mathematical relationship then allows the calculation of the L solute descriptors of the remaining 149 methylated alkanes. These calculations are summarized in the last column of Table 1. As an informational note, Katritzky et al. identified the different alkanes by a numerical labelling scheme where the first two digits in the number indicated the length of the longest carbon chain, and each of the next two-digit pairs showed the location of the methyl substituent on the carbon-atom backbone. We named the compounds labelled 22_0822 and 38_162024 as 8-methyltricosane and 15,19,23-trimethyloctatriacontane, respectively. For the first alkane, the placement of a methyl substituent on the 22nd carbon atom would increase the carbon backbone by one carbon atom. For the second alkane, we renumbered the carbon atoms starting at the other end of the carbon backbone to obtain a smaller set of numerical values.

3. Calculation of Thermodynamic Properties of Large Methylated Alkanes Using Abraham Model Solute Descriptors

The L solute descriptors that are tabulated in the last column of Table 1 provide researchers with an additional 149 chemical compounds to use in developing group contribution and machine learning methods for predicting Abraham model solute descriptors. Remember that the E, S, A and B solute descriptors of the tabulated compounds are equal to zero, and that the V solute descriptor values can be easily obtained using the method described by Abraham and McGowan [73]. The tabulated values given in Table 1 can also be used in conjunction with published Abraham model correlations to predict a wide range of physical, biological and thermodynamic properties including vapor pressures, enthalpies of vaporization and sublimation, enthalpies of solvation, aquatic toxicities and other properties. In the next few paragraphs, we will illustrate the computational methodology by calculating the standard molar enthalpies of sublimation, ΔHsub,298K, and of vaporization at 298 K, ΔHvap,298K, as well as discussing how the former values might be combined with measured enthalpy of solution data, ΔHsoln,298K, to obtain a second set of predicted ΔHsub,298K values. While our computations are focused on the large, methylated alkanes studied in the current communication, we note that the computational method can be applied to other organic compounds as well. All that is needed for the predictions is knowledge of the Abraham model solute descriptors for the given compound and the Abraham model correlation for the property/process that one wishes to predict. This is the driving force behind the development of group contribution and machine learning methods to predict Abraham model solute descriptors.
For the methylated alkane compounds studied in the current communication, the numerical values of ΔHsub,298K are calculated according to Equation (6) [46].
ΔHsub,298K = 13.93 + 13.57 L − 0.05 L × L
For the convenience of the journal readers, we have removed the ek × E, sk × S, ak × A and bk × B terms from Equation (2) as these terms will not contribute to the calculated ΔHsub,298K values because the E, S, A and B solute descriptors of the methylated alkane compounds are set equal to zero. The second column in Table 2 contains our calculated ΔHsub,298K values for the 178 compounds gathered from the Katritzky et al. [72] paper.
In our search of the published chemical and engineering literature we did not find experimental ΔHsub,298K data to compare our calculated values against. The sublimation enthalpies of large, nonvolatile compounds are difficult to measure due to the compound’s very small vapor pressures; however, these quantities are often needed in the design of high-temperature industrial processes and in the calculation of gas-phase standard molar enthalpies of formation from enthalpy of combustion measurements. What we offer in the way of a comparison is to compare our Abraham model predictions against the calculated values from the Naef and Acree group-additivity method [14]. The group-additivity method has been shown to predict ΔHsub,298K values for approximately 1866 molecular compounds to within a standard deviation of SD = 10.33 kJ mol−1. The basic method estimates a given thermodynamic or physical property by:
P r o p e r t y =   i A i a i + j B j b j + C o n s t a n t
summing the contributions that each individual atom group makes to the overall property. In Equation (7), Ai denotes the number of occurrences of the ith atom group, Bj is the number of times each special group occurs, and ai and bj are the numerical values of each atom group and special group.
For monomethylated and polymethylated alkanes, the atom group-additivity method proposed by Naef and Acree [14] fragments molecules into three distinct kinds of sp3 hybridized carbon atoms based on the number of each type of atoms directly bonded to the carbon atom. The first carbon-atom group will be bonded to three hydrogen atoms and one carbon atom (CH3 group), the second carbon-atom group will be attached to two hydrogen and two carbon atoms (CH2 group), and the third carbon-atom group has a single hydrogen and three carbon-atom nearest neighbors (CH group). The method also includes one special group that is defined as the total number of carbon atoms in the alkane molecule.
In Equation (8) below we have inserted the numerical group values and constants into Equation (7) for predicting ΔHsub,298K of CnH2n+2 monomethylated and polymethylated alkanes:
ΔHsub,298K (kJ mol−1) = 5.99 nCH3 + 6.88 nCH2 + 2.28 nCH − 0.53 ncarbons + 21.03
We note that the predicted values based on Equation (6) of the Abraham model are similar to the predictions based on the group-additivity model of Naef and Acree [14] for the “smaller” of the large polymethylated alkanes as shown by the numerical entries in the last two columns of Table 2. The differences become more pronounced with increasing carbon-atom chain length. The group-additivity method is unable to distinguish between the placement of the alkyl-substituent group along the large carbon-atom chain, and yields the same predicted values for a common set of number of different atom types. In other words, the predicted values of all dimethylhexacosane isomers in Table 2 are the same. Every dimethylhexacosane isomer considered in this study has 4 CH3-type carbon atoms, 22 CH2-type carbon atoms, 2 CH-type carbon atoms, and 28 total carbon atoms. The only dimethylhexacosane isomers that would be different would be those in which both methyl groups were situated on the same carbon atom. The predicted values of these latter dimethylhexacosane isomers would be identical to each other, but different from the dimethylhexacosane isomers in Table 2. Identical predicted values for isomeric compounds are a common feature of most published group-additivity and group contribution methods for predicting thermodynamic properties of organic compounds. The Abraham model, on the other hand, will give different predicted values for each dimethylhexacosane isomer, and does not require that the molecule be fragmented into atom groups or functional groups.
The enthalpies of vaporization would be calculated in similar fashion using the mathematical correlation developed by Churchill and coworkers [45]:
ΔHvap,298K (kJ mol−1) = 6.100 + 9.537 L
and the group-additivity method proposed by Naef and Acree [14]:
ΔHvap,298K (kJ mol−1) = 3.07 nCH3 + 4.67 nCH2 + 3.57 nCH + 0.09 ncarbons + 8.61
As before, only the terms needed in the calculation of the ΔHvap,298K values for the polymethylated alkanes studied in the current communication are given. The standard molar enthalpies of vaporization of large alkanes can be experimentally determined using correlation gas chromatography [74,75,76]. The experimental method is applicable to both solid and liquid compounds, and moreover, does not require highly purified chemical samples as the chromatographic retention times corresponding to the dissolved impurities in the samples can be distinguished from the desired chemical compound by their much smaller peak areas.
Solomonov and coworkers [77,78,79,80,81] recently devised an indirect method for determining both standard molar enthalpies of vaporization and sublimation from measured enthalpies of solution, ΔHsoln, and predicted enthalpies of solvation, ΔHsolv, for the given chemical compound dissolved in a suitable organic solvent. Numerical values of ΔHvap,298K and ΔHsub,298K were calculated from:
ΔHvap,298K = ΔHsoln,298K − ΔHsolv,298K
ΔHsub,298K = ΔHsoln,298K − ΔHsolv,298K
Equations (11) and (12), respectively, depending upon whether the dissolved solute is a liquid or crystalline compound. The standard molar vaporization/sublimation enthalpies of vaporization and sublimation based upon the proposed solution calorimetry approach of Solomonov and coworkers were found to be in good agreement (within experimental uncertainties) with the values determined by the more direct calorimetric, gas saturation and vapor pressure methods. The Abraham general solvation model was one of the predictive methods used by the authors [81] to calculate the solvation enthalpies. Abraham model correlations are available for calculating ΔHsolv, values for solutes dissolved in water and in more than 30 different organic solvents of varying polarity and hydrogen-bonding character. Group contribution and atom-additivity methods for predicting enthalpies of solvation are currently available for only a handful of organic solvents. In Table 3 we have tabulated the ΔHsolv values for 178 different polymethylated alkanes dissolved in benzene based upon:
ΔHsolv,298K (kJ mol−1) = −5.175(0.354) − 8.393(0.103) L
the updated Abraham model correlation reported by Lu et al. [82] The above correlation contains only the terms needed to predict values for the compounds studied in the current communication.

4. Conclusions

The current study is a continuation of our ongoing research involving the calculation Abraham model solute descriptors based on experimental water-to-organic solvent partition coefficients, infinite dilution activity coefficients, molar solubilities and gas–liquid chromatographic and high-performance liquid chromatographic retention data. Abraham model L solute descriptors have been calculated for an additional 149 C11 to C42 monomethylated and polymethylated alkanes based on the measured Kovat’s gas–liquid chromatographic retention indices retrieved from the published chemical literature. The calculated solute descriptors, in combination with previously published Abraham model correlations, can be used to predict a number of very important chemical and thermodynamic properties including partition coefficients, molar solubility ratios, gas–liquid chromatographic and HPLC retention data, infinite dilution activity coefficients, molar enthalpies of solvation, standard molar vaporization and sublimation at 298 K, vapor pressures, and limiting diffusion coefficients. The predictive computations are illustrated by estimating both the standard molar enthalpies of sublimation and the enthalpies of solvation in benzene for the monomethylated and polymethylated alkanes considered in the current study. The standard molar enthalpy of sublimation predictions were also performed using the group-additivity method proposed by Naef and Acree. Experimental thermodynamic data are not currently available for many of the larger monomethylated and polymethylated alkanes. Predictive methods provide practicing chemists and engineers working in the industrial manufacturing sector with a means to estimate the physical and thermodynamic properties needed in process design calculations.
A comparison of the two methods revealed that the ΔHsub,298K predictions based on the Abraham model are similar to predictions based on the group-additivity model of Naef and Acree [14] for the “smaller” of the large polymethylated alkanes. The differences became more pronounced with increasing carbon-atom chain length. The group-additivity method was not able to distinguish between the placement of the alkyl-substituent group attached to the large carbon-atom chain, and yielded the same predicted values for a given molecular formula. In other words, the predicted values of all dimethylhexacosane isomers were the same. This limitation is a common feature of most group-additivity and group contribution methods. The Abraham model, on the other hand, provides different predicted values for the different dimethylhexacosane molecules, and does not require fragmentation of the molecule into atom groups or functional groups.
The solute descriptors determined in the current study further the development of group contribution and machine learning methods by providing experimental-based values for an additional 149 chemical compounds. Published group contribution [53,54,55,56] and machine learning methods [55,56] have shown some promise along these lines in that the estimated descriptor values provide reasonably accurate predictions for both the molar enthalpies of solvation (ΔHsolv) and molar Gibbs energies of solvation (ΔGsolv) of organic solutes and inorganic gases in a wide range of organic solvents of varying polarity and hydrogen-bonding character.

Author Contributions

Conceptualization, writing—original draft preparation, W.E.A.J.; formal data analysis, E.W., S.S., C.Y. and M.Z.; writing—review and editing, E.W., S.S., C.Y. and M.Z. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Data is contained within the article.

Acknowledgments

Emily Wu, Sneha Sinha, Chelsea Yang and Miles Zhang thank the University of North Texas’s Texas Academy of Mathematics & Science (TAMS) program for providing a summer research scholarship to each student.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Graphical plot of the L solute descriptors versus (KRI/100) data for the 63 compounds used in the least-squares regression analysis for obtaining Equation (5).
Figure 1. Graphical plot of the L solute descriptors versus (KRI/100) data for the 63 compounds used in the least-squares regression analysis for obtaining Equation (5).
Liquids 02 00007 g001
Table 1. Kovat’s retention indices, KRI, and Abraham model L solute descriptors for linear alkanes and for methylated alkanes.
Table 1. Kovat’s retention indices, KRI, and Abraham model L solute descriptors for linear alkanes and for methylated alkanes.
Compound NameKRI/100L Value DatabaseL Value Calculated
Linear Alkanes
Heptane7.0003.1733.172
Octane8.0003.6773.676
Nonane9.0004.1824.180
Decane10.0004.6864.684
Undecane11.0005.1915.188
Dodecane12.0005.6965.692
Tridecane13.0006.2006.196
Tetradecane14.0006.7056.700
Pentadecane15.0007.2097.204
Hexadecane16.0007.7147.708
Heptadecane17.0008.2188.212
Octadecane18.0008.7228.716
Nonadecane19.0009.2269.220
Eicosane20.0009.7319.724
Heneicosane21.00010.23610.228
Docosane22.00010.74010.732
Tricosane23.00011.25211.236
Tetracosane24.00011.75811.740
Pentacosane25.00012.26412.244
Hexacosane26.00012.77012.748
Heptacosane27.00013.27613.252
Octacosane28.00013.78013.756
Nonacosane29.00014.29114.260
Triacontane30.00014.79414.764
Hentriacontane31.00015.32115.268
Dotriacontane32.00015.78715.772
Tritriacontane33.00016.30316.276
Tetratriacontane34.00016.81816.780
Pentatriacontane35.00017.22317.284
Hexatriacontane36.00017.73617.788
Heptatriacontane37.00018.21118.292
Octatriacontane38.00018.68618.796
Nonatriacontane39.00019.27019.300
Tetracontane40.00019.85319.804
Monomethylalkanes
2-Methylnonane9.6654.4534.515
3-Methylnonane9.7304.4864.548
2-Methylundecane11.6655.5165.523
3-Methylundecane11.7255.5505.553
2-Methyltridecane13.6656.5286.531
3-Methyltridecane13.7306.5636.564
2-Methylpentadecane15.6657.5397.539
3-Methylpentadecane15.7377.5777.575
2-Methylheptadecane17.6588.5518.544
3-Methylheptadecane17.7408.5918.585
2-Methylnonadecane19.6609.5639.553
3-Methylnonadecane19.7439.6079.594
10-Methylnonadecane19.4309.4499.437
2-Methylheneicosane21.66010.57110.561
3-Methylheneicosane21.74510.62110.603
11-Methylheneicosane21.41010.44910.435
2-Methyltricosane23.64011.58611.559
3-Methyltricosane23.74511.63511.611
8-Methyltricosane23.67011.46811.574
12-Methyltricosane23.37011.44911.422
2-Methylpentacosane25.63012.59912.562
3-Methylpentacosane25.74412.65112.619
13-Methylpentacosane25.34512.45412.418
2-Methylheptacosane27.63013.61113.570
3-Methylheptacosane27.74413.66613.627
14-Methylheptacosane27.33013.45813.418
2-Methylnonacosane29.62214.62614.573
3-Methylnonacosane29.74014.68014.633
15-Methylnonacosane29.31514.46414.419
2-Methylhentriacontane31.615 15.578
3-Methylhentriacontane31.741 15.641
4-Methylhentriacontane31.575 15.558
5-Methylhentriacontane31.500 15.520
6-Methylhentriacontane31.432 15.486
7-Methylhentriacontane31.400 15.470
13-Methylhentriacontane31.308 15.423
16-Methylhentriacontane31.298 15.418
2-Methyltritriacontane33.620 16.588
3-Methyltritriacontane33.745 16.651
4-Methyltritriacontane33.575 16.566
5-Methyltritriacontane33.500 16.528
6-Methyltritriacontane33.437 16.496
13-Methyltritriacontane33.285 16.420
17-Methyltritriacontane33.285 16.420
2-Methylpentatriacontane35.620 17.596
3-Methylpentatriacontane35.743 17.658
18-Methylpentatriacontane35.273 17.422
Dimethylalkanes
3,9-Dimethyltricosane24.100 11.790
5,9-Dimethyltetracosane24.850 12.168
3,11-Dimethylpentacosane26.090 12.793
3,15-Dimethylpentacosane26.050 12.773
5,11-Dimethylpentacosane25.820 12.657
5,17-Dimethylpentacosane25.850 12.672
7,11-Dimethylpentacosane25.770 12.632
2,6-Dimethylhexacosane27.040 13.272
4,8-Dimethylhexacosane26.950 13.227
5,11-Dimethylhexacosane26.820 13.161
6,10-Dimethylhexacosane26.780 13.141
7,11-Dimethylhexacosane26.750 13.126
3,7-Dimethylheptacosane28.090 13.801
3,15-Dimethylheptacosane28.050 13.781
5,11-Dimethylheptacosane27.820 13.665
5,17-Dimethylheptacosane27.860 13.685
7,13-Dimethylheptacosane27.740 13.625
9,19-Dimethylheptacosane27.650 13.580
2,6-Dimethyloctacosane29.050 14.285
2,10-Dimethyloctacosane28.990 14.255
4,10-Dimethyloctacosane28.950 14.235
5,15-Dimethyloctacosane28.820 14.169
7,13-Dimethyloctacosane28.730 14.124
3,7-Dimethylnonacosane30.080 14.804
3,13-Dimethylnonacosane30.040 14.784
5,13-Dimethylnonacosane29.820 14.673
5,19-Dimethylnonacosane29.830 14.678
7,17-Dimethylnonacosane29.730 14.628
2,6-Dimethyltriacontane31.050 15.293
2,10-Dimethyltriacontane30.990 15.263
2,12-Dimethyltriacontane30.950 15.243
3,7-Dimethyltriacontane31.080 15.308
4,10-Dimethyltriacontane30.940 15.238
6,10-Dimethyltriacontane30.750 15.142
3,7-Dimethylhentriacontane32.090 15.817
3,13-Dimethylhentriacontane32.030 15.787
3,15-Dimethylhentriacontane32.090 15.817
5,13-Dimethylhentriacontane31.805 15.674
5,17-Dimethylhentriacontane31.820 15.681
7,11-Dimethylhentriacontane31.702 15.622
11,21-Dimethylhentriacontane31.629 15.585
2,8-Dimethyldotriacontane32.970 16.261
4,8-Dimethyldotriacontane32.920 16.236
6,10-Dimethyldotriacontane32.730 16.140
8,12-Dimethyldotriacontane32.660 16.105
9,21-Dimethyldotriacontane32.620 16.084
14,18-Dimethyldotriacontane32.575 16.062
3,9-Dimethyltritriacontane34.030 16.795
3,15-Dimethyltritriacontane34.090 16.825
5,16-Dimethyltritriacontane33.800 16.679
5,19-Dimethyltritriacontane33.820 16.689
7,17-Dimethyltritriacontane33.700 16.629
11,23-Dimethyltritriacontane33.624 16.590
2,10-Dimethyltetratriacontane34.940 17.254
4,16-Dimethyltetratriacontane34.890 17.229
6,10-Dimethyltetratriacontane34.738 17.152
8,12-Dimethyltetratriacontane34.650 17.108
12,22-Dimethyltetratriacontane34.614 17.089
13,17-Dimethyltetratriacontane34.550 17.057
3,7-Dimethylpentatriacontane36.095 17.836
3,15-Dimethylpentatriacontane36.010 17.793
5,9-Dimethylpentatriacontane35.800 17.687
5,19-Dimethylpentatriacontane35.805 17.690
7,17-Dimethylpentatriacontane35.697 17.635
9,21-Dimethylpentatriacontane35.610 17.591
2,12-Dimethylhexatriacontane36.950 18.267
5,17-Dimethylhexatriacontane36.800 18.191
13,23-Dimethylhexatriacontane36.610 18.095
3,15-Dimethylheptatriacontane38.010 18.801
5,19-Dimethylheptatriacontane37.790 18.690
5,17-Dimethylheptatriacontane37.800 18.695
13,23-Dimethylheptatriacontane37.590 18.589
5,17-Dimethyloctatriacontane38.780 19.189
Trimethylalkanes
4,8,12-Trimethyltetracosane25.200 12.345
5,9,13-Trimethylpentacosane26.100 12.798
4,8,12-Trimethylhexacosane27.190 13.348
3,7,11-Trimethylheptacosane28.380 13.948
4,8,12-Trimethyloctacosane29.180 14.351
3,7,11-Trimethylnonacosane30.370 14.950
5,13,17-Trimethylnonacosane30.070 14.799
6,14,18-Trimethyltriacontane31.000 15.268
3,7,11-Trimethylhentriacontane32.365 15.956
5,13,17-Trimethylhentriacontane32.054 15.799
7,13,17-Trimethylhentriacontane31.913 15.728
11,15,19-Trimethylhentriacontane31.810 15.676
2,10,16-Trimethyldotriacontane33.240 16.397
4,12,16-Trimethyldotriacontane33.160 16.357
6,14,18-Trimethyldotriacontane32.990 16.271
12,16,20-Trimethyldotriacontane32.810 16.180
3,7,15-Trimethyltritriacontane34.365 16.964
5,13,17-Trimethyltritriacontane34.050 16.805
7,11,15-Trimethyltritriacontane33.890 16.725
11,15,19-Trimethyltritriacontane33.796 16.677
2,10,16-Trimethyltetratriacontane35.240 17.405
4,8,12-Trimethyltetratriacontane35.155 17.362
6,14,18-Trimethyltetratriacontane34.970 17.269
8,12,16-Trimethyltetratriacontane34.864 17.215
12,16,20-Trimethyltetratriacontane34.780 17.173
3,7,15-Trimethylpentatriacontane36.363 17.971
5,9,13-Trimethylpentatriacontane36.050 17.813
7,11,15-Trimethylpentatriacontane35.883 17.729
13,17,21-Trimethylpentatriacontane35.770 17.672
13,17,23-Trimethylpentatriacontane35.830 17.702
4,8,16-Trimethylhexatriacontane37.150 18.368
8,12,16-Trimethylhexatriacontane36.850 18.216
14,18,22-Trimethylhexatriacontane36.760 18.171
3,7,15-Trimethylheptatriacontane38.350 18.972
5,13,17-Trimethylheptatriacontane38.030 18.811
7,13,19-Trimethylheptatriacontane37.840 18.715
15,19,23-Trimethylheptatriacontane37.750 18.670
15,19,23-Trimethyloctatriacontane38.735 19.166
5,13,17-Trimethylnonatriacontane40.010 19.809
15,19,23-Trimethylnonatriacontane39.724 19.665
14,18,22-Trimethyltetracontane40.710 20.162
Tetramethylalkanes
3,7,11,15-Tetramethylnonacosane30.620 15.076
3,7,11,15-Tetramethylhentriacontane32.610 16.079
4,8,12,16-Tetramethylhentriacontane32.490 16.019
3,7,11,15-Tetramethyltritriacontane34.590 17.077
4,8,12,16-Tetramethyltritriacontane34.480 17.022
3,7,11,15-Tetramethylpentatriacontane36.580 18.080
7,11,15,19-Tetramethylpentatriacontane36.280 17.929
9,13,17,21-Tetramethylpentatriacontane36.170 17.874
11,15,19,24-Tetramethylpentatriacontane36.050 17.813
6,10,12,16-Tetramethylhexatriacontane37.230 18.408
8,12,16,20-Tetramethylhexatriacontane37.130 18.358
10,14,18,22-Tetramethylhexatriacontane37.035 18.310
3,7,11,15-Tetramethylheptatriacontane38.550 19.073
7,11,15,19-Tetramethylheptatriacontane38.230 18.912
9,13,17,21-Tetramethylheptatriacontane38.130 18.862
11,15,19,24-Tetramethylheptatriacontane38.030 18.811
10,14,18,22-Tetramethyloctatriacontane39.000 19.300
Table 2. Comparison of the enthalpies of sublimation, ΔHsub,298K (in kJ mol−1), predicted by the Abraham model Equation (6) and the group-additivity method of Naef and Acree (Equation (8)).
Table 2. Comparison of the enthalpies of sublimation, ΔHsub,298K (in kJ mol−1), predicted by the Abraham model Equation (6) and the group-additivity method of Naef and Acree (Equation (8)).
Compound NameΔHsub,298K
Equation (6)
ΔHsub,298K
Equation (8)
Monomethylalkanes
2-Methylnonane73.477.3
3-Methylnonane73.877.3
2-Methylundecane87.390.0
3-Methylundecane87.790.0
2-Methyltridecane100.4102.7
3-Methyltridecane100.8102.7
2-Methylpentadecane113.4115.4
3-Methylpentadecane113.9115.4
2-Methylheptadecane126.3128.1
3-Methylheptadecane126.8128.1
2-Methylnonadecane139.1140.8
3-Methylnonadecane139.7140.8
10-Methylnonadecane137.7140.8
2-Methylheneicosane151.8153.5
3-Methylheneicosane152.4153.5
11-Methylheneicosane150.3153.5
2-Methyltricosane164.4166.2
3-Methyltricosane165.1166.2
8-Methyltricosane163.0166.2
12-Methyltricosane162.7166.2
2-Methylpentacosane177.0178.9
3-Methylpentacosane177.6178.9
13-Methylpentacosane175.2178.9
2-Methylheptacosane189.4191.6
3-Methylheptacosane190.0191.6
14-Methylheptacosane187.5191.6
2-Methylnonacosane201.7204.3
3-Methylnonacosane202.4204.3
15-Methylnonacosane199.8204.3
2-Methylhentriacontane213.2217.0
3-Methylhentriacontane214.0217.0
4-Methylhentriacontane213.0217.0
5-Methylhentriacontane212.5217.0
6-Methylhentriacontane212.1217.0
7-Methylhentriacontane211.9217.0
13-Methylhentriacontane211.3217.0
16-Methylhentriacontane211.3217.0
2-Methyltritriacontane225.3229.7
3-Methyltritriacontane226.0229.7
4-Methyltritriacontane225.0229.7
5-Methyltritriacontane224.6229.7
6-Methyltritriacontane224.2229.7
13-Methyltritriacontane223.3229.7
17-Methyltritriacontane223.3229.7
2-Methylpentatriacontane237.2242.4
3-Methylpentatriacontane238.0242.4
18-Methylpentatriacontane235.2242.4
Dimethylalkanes
3,9-Dimethyltricosane167.0167.0
5,9-Dimethyltetracosane171.7173.4
3,11-Dimethylpentacosane179.4179.7
3,15-Dimethylpentacosane179.1179.7
5,11-Dimethylpentacosane177.7179.7
5,17-Dimethylpentacosane177.9179.7
7,11-Dimethylpentacosane177.4179.7
2,6-Dimethylhexacosane185.2186.1
4,8-Dimethylhexacosane184.7186.1
5,11-Dimethylhexacosane183.9186.1
6,10-Dimethylhexacosane183.6186.1
7,11-Dimethylhexacosane183.4186.1
3,7-Dimethylheptacosane191.7192.4
3,15-Dimethylheptacosane191.4192.4
5,11-Dimethylheptacosane190.0192.4
5,17-Dimethylheptacosane190.3192.4
7,13-Dimethylheptacosane189.5192.4
9,19-Dimethylheptacosane189.0192.4
2,6-Dimethyloctacosane197.6198.8
2,10-Dimethyloctacosane197.2198.8
4,10-Dimethyloctacosane197.0198.8
5,15-Dimethyloctacosane196.2198.8
7,13-Dimethyloctacosane195.6198.8
3,7-Dimethylnonacosane203.9205.1
3,13-Dimethylnonacosane203.6205.1
5,13-Dimethylnonacosane202.3205.1
5,19-Dimethylnonacosane202.3205.1
7,17-Dimethylnonacosane201.7205.1
2,6-Dimethyltriacontane209.8211.5
2,10-Dimethyltriacontane209.4211.5
2,12-Dimethyltriacontane209.2211.5
3,7-Dimethyltriacontane210.0211.5
4,10-Dimethyltriacontane209.1211.5
6,10-Dimethyltriacontane207.9211.5
3,7-Dimethylhentriacontane216.1217.8
3,13-Dimethylhentriacontane215.7217.8
3,15-Dimethylhentriacontane216.1217.8
5,13-Dimethylhentriacontane214.3217.8
5,17-Dimethylhentriacontane214.4217.8
7,11-Dimethylhentriacontane213.7217.8
11,21-Dimethylhentriacontane213.3217.8
2,8-Dimethyldotriacontane221.4224.2
4,8-Dimethyldotriacontane221.1224.2
6,10-Dimethyldotriacontane219.9224.2
8,12-Dimethyldotriacontane219.5224.2
9,21-Dimethyldotriacontane219.3224.2
14,18-Dimethyldotriacontane219.0224.2
3,9-Dimethyltritriacontane227.7230.5
3,15-Dimethyltritriacontane228.1230.5
5,16-Dimethyltritriacontane226.4230.5
5,19-Dimethyltritriacontane226.5230.5
7,17-Dimethyltritriacontane225.8230.5
11,23-Dimethyltritriacontane225.3230.5
2,10-Dimethyltetratriacontane233.2236.9
4,16-Dimethyltetratriacontane232.9236.9
6,10-Dimethyltetratriacontane232.0236.9
8,12-Dimethyltetratriacontane231.5236.9
12,22-Dimethyltetratriacontane231.2236.9
13,17-Dimethyltetratriacontane230.9236.9
3,7-Dimethylpentatriacontane240.1243.2
3,15-Dimethylpentatriacontane239.6243.2
5,9-Dimethylpentatriacontane238.3243.2
5,19-Dimethylpentatriacontane238.3243.2
7,17-Dimethylpentatriacontane237.7243.2
9,21-Dimethylpentatriacontane237.2243.2
2,12-Dimethylhexatriacontane245.1249.6
5,17-Dimethylhexatriacontane244.2249.6
13,23-Dimethylhexatriacontane243.1249.6
3,15-Dimethylheptatriacontane251.4255.9
5,19-Dimethylheptatriacontane250.1255.9
5,17-Dimethylheptatriacontane250.2255.9
13,23-Dimethylheptatriacontane248.9255.9
5,17-Dimethyloctatriacontane255.9262.3
Trimethylalkanes
4,8,12-Trimethyltetracosane173.8174.2
5,9,13-Trimethylpentacosane179.4180.6
4,8,12-Trimethylhexacosane186.2186.9
3,7,11-Trimethylheptacosane193.5193.3
4,8,12-Trimethyloctacosane198.4199.6
3,7,11-Trimethylnonacosane205.6206.0
5,13,17-Trimethylnonacosane203.8206.0
6,14,18-Trimethyltriacontane209.5212.3
3,7,11-Trimethylhentriacontane217.7218.7
5,13,17-Trimethylhentriacontane215.8218.7
7,13,17-Trimethylhentriacontane215.0218.7
11,15,19-Trimethylhentriacontane214.4218.7
2,10,16-Trimethyldotriacontane223.0225.0
4,12,16-Trimethyldotriacontane222.5225.0
6,14,18-Trimethyldotriacontane221.5225.0
12,16,20-Trimethyldotriacontane220.4225.0
3,7,15-Trimethyltritriacontane229.7231.4
5,13,17-Trimethyltritriacontane227.9231.4
7,11,15-Trimethyltritriacontane226.9231.4
11,15,19-Trimethyltritriacontane226.3231.4
2,10,16-Trimethyltetratriacontane235.0237.7
4,8,12-Trimethyltetratriacontane234.5237.7
6,14,18-Trimethyltetratriacontane233.4237.7
8,12,16-Trimethyltetratriacontane232.7237.7
12,16,20-Trimethyltetratriacontane232.2237.7
3,7,15-Trimethylpentatriacontane241.7244.1
5,9,13-Trimethylpentatriacontane239.8244.1
7,11,15-Trimethylpentatriacontane238.8244.1
13,17,21-Trimethylpentatriacontane238.1244.1
13,17,23-Trimethylpentatriacontane238.5244.1
4,8,16-Trimethylhexatriacontane246.3250.4
8,12,16-Trimethylhexatriacontane244.5250.4
14,18,22-Trimethylhexatriacontane244.0250.4
3,7,15-Trimethylheptatriacontane253.4256.8
5,13,17-Trimethylheptatriacontane251.5256.8
7,13,19-Trimethylheptatriacontane250.4256.8
15,19,23-Trimethylheptatriacontane249.9256.8
15,19,23-Trimethyloctatriacontane255.7263.1
5,13,17-Trimethylnonatriacontane263.1269.5
15,19,23-Trimethylnonatriacontane261.5269.5
14,18,22-Trimethyltetracontane267.2275.8
Tetramethylalkanes
3,7,11,15-Tetramethylnonacosane207.2206.8
3,7,11,15-Tetramethylhentriacontane219.2219.5
4,8,12,16-Tetramethylhentriacontane218.5219.5
3,7,11,15-Tetramethyltritriacontane231.1232.2
4,8,12,16-Tetramethyltritriacontane230.4232.2
3,7,11,15-Tetramethylpentatriacontane242.9244.9
7,11,15,19-Tetramethylpentatriacontane241.2244.9
9,13,17,21-Tetramethylpentatriacontane240.5244.9
11,15,19,24-Tetramethylpentatriacontane239.8244.9
6,10,12,16-Tetramethylhexatriacontane246.8251.3
8,12,16,20-Tetramethylhexatriacontane246.2251.3
10,14,18,22-Tetramethylhexatriacontane245.6251.3
3,7,11,15-Tetramethylheptatriacontane254.6257.6
7,11,15,19-Tetramethylheptatriacontane252.7257.6
9,13,17,21-Tetramethylheptatriacontane252.1257.6
11,15,19,24-Tetramethylheptatriacontane251.5257.6
10,14,18,22-Tetramethyloctatriacontane257.2264.0
Table 3. Predicted gas-to-benzene enthalpies of solvation, ΔHsolv,298K (in kJ mol−1) for 178 monomethylated and polymethylated alkanes based upon Equation (13).
Table 3. Predicted gas-to-benzene enthalpies of solvation, ΔHsolv,298K (in kJ mol−1) for 178 monomethylated and polymethylated alkanes based upon Equation (13).
Compound NameΔHsolv,298K (kJ mol−1)Compound NameΔHsolv,298K (kJ mol−1)
Monomethylalkanes Dimethylalkanes
2-Methylnonane−42.63,9-Dimethyltricosane−104.1
3-Methylnonane−42.85,9-Dimethyltetracosane−107.3
2-Methylundecane−51.53,11-Dimethylpentacosane−112.6
3-Methylundecane−51.83,15-Dimethylpentacosane−112.4
2-Methyltridecane−60.05,11-Dimethylpentacosane−111.4
3-Methyltridecane−60.35,17-Dimethylpentacosane−111.5
2-Methylpentadecane−68.57,11-Dimethylpentacosane−111.2
3-Methylpentadecane−68.82,6-Dimethylhexacosane−116.6
2-Methylheptadecane−76.94,8-Dimethylhexacosane−116.2
3-Methylheptadecane−77.35,11-Dimethylhexacosane−115.6
2-Methylnonadecane−85.46,10-Dimethylhexacosane−115.5
3-Methylnonadecane−85.87,11-Dimethylhexacosane−115.3
10-Methylnonadecane−84.53,7-Dimethylheptacosane−121.0
2-Methylheneicosane−93.93,15-Dimethylheptacosane−120.8
3-Methylheneicosane−94.35,11-Dimethylheptacosane−119.9
11-Methylheneicosane−92.95,17-Dimethylheptacosane−120.0
2-Methyltricosane−102.47,13-Dimethylheptacosane−119.5
3-Methyltricosane−102.89,19-Dimethylheptacosane−119.2
8-Methyltricosane−101.42,6-Dimethyloctacosane−125.1
12-Methyltricosane−101.32,10-Dimethyloctacosane−124.8
2-Methylpentacosane−110.94,10-Dimethyloctacosane−124.7
3-Methylpentacosane−111.45,15-Dimethyloctacosane−124.1
13-Methylpentacosane−109.77,13-Dimethyloctacosane−123.7
2-Methylheptacosane−119.43,7-Dimethylnonacosane−129.4
3-Methylheptacosane−119.93,13-Dimethylnonacosane−129.3
14-Methylheptacosane−118.15,13-Dimethylnonacosane−128.3
2-Methylnonacosane−127.95,19-Dimethylnonacosane−128.4
3-Methylnonacosane−128.47,17-Dimethylnonacosane−128.0
15-Methylnonacosane−126.62,6-Dimethyltriacontane−133.5
2-Methylhentriacontane−135.92,10-Dimethyltriacontane−133.3
3-Methylhentriacontane−136.52,12-Dimethyltriacontane−133.1
4-Methylhentriacontane−135.83,7-Dimethyltriacontane−133.7
5-Methylhentriacontane−135.44,10-Dimethyltriacontane−133.1
6-Methylhentriacontane−135.26,10-Dimethyltriacontane−132.3
7-Methylhentriacontane−135.03,7-Dimethylhentriacontane−137.9
13-Methylhentriacontane−134.63,13-Dimethylhentriacontane−137.7
16-Methylhentriacontane−134.63,15-Dimethylhentriacontane−137.9
2-Methyltritriacontane−144.45,13-Dimethylhentriacontane−136.7
3-Methyltritriacontane−144.95,17-Dimethylhentriacontane−136.8
4-Methyltritriacontane−144.27,11-Dimethylhentriacontane−136.3
5-Methyltritriacontane−143.911,21-Dimethylhentriacontane−136.0
6-Methyltritriacontane−143.62,8-Dimethyldotriacontane−141.7
13-Methyltritriacontane−143.04,8-Dimethyldotriacontane−141.4
17-Methyltritriacontane−143.06,10-Dimethyldotriacontane−140.6
2-Methylpentatriacontane−152.98,12-Dimethyldotriacontane−140.3
3-Methylpentatriacontane−153.49,21-Dimethyldotriacontane−140.2
18-Methylpentatriacontane−151.414,18-Dimethyldotriacontane−140.0
Trimethylalkane 3,9-Dimethyltritriacontane−146.1
4,8,12-Trimethyltetracosane−108.83,15-Dimethyltritriacontane−146.4
5,9,13-Trimethylpentacosane−112.65,16-Dimethyltritriacontane−145.2
4,8,12-Trimethylhexacosane−117.25,19-Dimethyltritriacontane−145.3
3,7,11-Trimethylheptacosane−122.27,17-Dimethyltritriacontane−144.7
4,8,12-Trimethyloctacosane−125.611,23-Dimethyltritriacontane−144.4
3,7,11-Trimethylnonacosane−130.72,10-Dimethyltetratriacontane−150.0
5,13,17-Trimethylnonacosane−129.44,16-Dimethyltetratriacontane−149.8
6,14,18-Trimethyltriacontane−133.36,10-Dimethyltetratriacontane−149.1
3,7,11-Trimethylhentriacontane−139.18,12-Dimethyltetratriacontane−148.8
5,13,17-Trimethylhentriacontane−137.812,22-Dimethyltetratriacontane−148.6
7,13,17-Trimethylhentriacontane−137.213,17-Dimethyltetratriacontane−148.3
11,15,19-Trimethylhentriacontane−136.83,7-Dimethylpentatriacontane−154.9
2,10,16-Trimethyldotriacontane−142.83,15-Dimethylpentatriacontane−154.5
4,12,16-Trimethyldotriacontane−142.55,9-Dimethylpentatriacontane−153.6
6,14,18-Trimethyldotriacontane−141.75,19-Dimethylpentatriacontane−153.6
12,16,20-Trimethyldotriacontane−141.07,17-Dimethylpentatriacontane−153.2
3,7,15-Trimethyltritriacontane−147.69,21-Dimethylpentatriacontane−152.8
5,13,17-Trimethyltritriacontane−146.22,12-Dimethylhexatriacontane−158.5
7,11,15-Trimethyltritriacontane−145.55,17-Dimethylhexatriacontane−157.9
11,15,19-Trimethyltritriacontane−145.213,23-Dimethylhexatriacontane−157.1
2,10,16-Trimethyltetratricontane−151.33,15-Dimethylheptatriacontane−163.0
4,8,12-Trimethyltetratriacontane−150.95,19-Dimethylheptatriacontane−162.0
6,14,18-Trimethyltetratriacontane−150.15,17-Dimethylheptatriacontane−162.1
8,12,16-Trimethyltetratriacontane−149.713,23-Dimethylheptatriacontane−161.2
12,16,20-Trimethyltetratriacontane−149.35,17-Dimethyloctatriacontane−166.2
3,7,15-Trimethylpentatriacontane−156.0Tetramethylalkane
5,9,13-Trimethylpentatriacontane−154.73,7,11,15-Tetramethylnonacosane−131.7
7,11,15-Trimethylpentatriacontane−154.03,7,11,15-Tetramethylhentriacontane−140.1
13,17,21-Trimethylpentatriacontane−153.54,8,12,16-Tetramethylhentriacontane−139.6
13,17,23-Trimethylpentatriacontane−153.83,7,11,15-Tetramethyltritriacontane−148.5
4,8,16-Trimethylhexatriacontane−159.34,8,12,16-Tetramethyltritriacontane−148.0
8,12,16-Trimethylhexatriacontane−158.13,7,11,15-Tetramethylpentatriacontane−156.9
14,18,22-Trimethylhexatriacontane−157.77,11,15,19-Tetramethylpentatriacontane−155.7
3,7,15-Trimethylheptatriacontane−164.49,13,17,21-Tetramethylpentatriacontane−155.2
5,13,17-Trimethylheptatriacontane−163.111,15,19,24-Tetramethylpentatriacontane−154.7
7,13,19-Trimethylheptatriacontane−162.36,10,12,16-Tetramethylhexatriacontane−159.8
15,19,23-Trimethylheptatriacontane−161.98,12,16,20-Tetramethylhexatriacontane−159.3
15,19,23-Trimethyloctatriacontane−166.010,14,18,22-Tetramethylhexatriacontane−158.9
5,13,17-Trimethylnonatriacontane−171.43,7,11,15-Tetramethylheptatriacontane−165.3
15,19,23-Trimethylnonatriacontane−170.27,11,15,19-Tetramethylheptatriacontane−163.9
14,18,22-Trimethyltetracontane−174.49,13,17,21-Tetramethylheptatriacontane−163.5
11,15,19,24-Tetramethylheptatriacontane−163.1
10,14,18,22-Tetramethyloctatriacontane−167.2
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MDPI and ACS Style

Wu, E.; Sinha, S.; Yang, C.; Zhang, M.; Acree, W.E., Jr. Abraham Solvation Parameter Model: Calculation of L Solute Descriptors for Large C11 to C42 Methylated Alkanes from Measured Gas–Liquid Chromatographic Retention Data. Liquids 2022, 2, 85-105. https://doi.org/10.3390/liquids2030007

AMA Style

Wu E, Sinha S, Yang C, Zhang M, Acree WE Jr. Abraham Solvation Parameter Model: Calculation of L Solute Descriptors for Large C11 to C42 Methylated Alkanes from Measured Gas–Liquid Chromatographic Retention Data. Liquids. 2022; 2(3):85-105. https://doi.org/10.3390/liquids2030007

Chicago/Turabian Style

Wu, Emily, Sneha Sinha, Chelsea Yang, Miles Zhang, and William E. Acree, Jr. 2022. "Abraham Solvation Parameter Model: Calculation of L Solute Descriptors for Large C11 to C42 Methylated Alkanes from Measured Gas–Liquid Chromatographic Retention Data" Liquids 2, no. 3: 85-105. https://doi.org/10.3390/liquids2030007

APA Style

Wu, E., Sinha, S., Yang, C., Zhang, M., & Acree, W. E., Jr. (2022). Abraham Solvation Parameter Model: Calculation of L Solute Descriptors for Large C11 to C42 Methylated Alkanes from Measured Gas–Liquid Chromatographic Retention Data. Liquids, 2(3), 85-105. https://doi.org/10.3390/liquids2030007

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