LFER solvent coefficients (data page)

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This page provides supplementary data and solvent coefficients for linear free-energy relationships.

Contents

Partition between water and organic solvents

The LFER used to obtain partition coefficients that uses the systems below takes the form log Ps = c + eE + sS + aA + bB + vV

Coefficients for partition between water and solvents
wet/drysolventcesabvsource
w 1-butanol 0.3760.434-0.718-0.097-2.3502.682 [1]
w 1-pentanol 0.1850.367-0.7320.105-3.1003.395 [1]
w 1-hexanol -0.0060.460-0.9400.142-3.2843.792 [1]
w 1-heptanol 0.0410.497-0.9760.030-3.4383.859 [1]
w 1-octanol 0.0880.562-1.0540.034-3.4603.814 [1]
w 1-nonanol -0.0410.562-1.1030.090-3.5403.922 [1]
w 1-decanol -0.1360.542-0.9890.046-3.7223.996 [1]
w isobutanol 0.2490.480-0.639-0.050-2.2842.758 [1]
w/d olely alcohol -0.0960.148-0.841-0.438-4.0404.125 [1]
w/d dichloromethane 0.3190.102-0.187-3.058-4.0904.324 [1]
w/dtrichloromethane0.1910.105-0.403-3.112-3.5144.395 [1]
w/dtetrachloromethane0.1990.523-1.159-3.560-4.5944.618 [1]
w/d1,2-dichloroethane0.1830.294-0.134-2.801-4.2914.180 [1]
w/d1-chlorobutane0.2220.273-0.569-2.918-4.8834.456 [1]
w/dbutane0.297-0.005-1.584-3.188-4.5674.562 [1]
w/dpentane0.3690.386-1.568-3.535-5.2154.514 [1]
w/dhexane0.3330.56-1.71-3.578-4.9394.463 [2]
w/dheptane0.2970.643-1.755-3.571-4.9464.488 [2]
w/doctane0.2310.738-1.84-3.585-4.9074.502 [2]
w/dnonane0.2400.619-1.713-3.532-4.9214.482 [1]
w/ddecane0.1860.722-1.741-3.449-4.974.476 [2]
w/dundecane0.0580.603-1.661-3.421-5.1204.619 [1]
w/ddodecane0.1140.668-1.644-3.545-5.0064.459 [1]
w/dhexadecane0.0870.667-1.617-3.587-4.8694.433 [1]
w/dcyclohexane0.1590.784-1.678-3.740-4.9294.577 [1]
w/dmethylcyclohexane0.2460.782-1.982-3.517-4.2934.528 [1]
w/disooctane0.320.511-1.685-3.687-4.8114.399 [3]
d1-hexadecene0.1160.706-1.616-3.181-4.7964.322 [4]
d1,9-decadiene0.1040.615-1.796-3.07-4.2914.518 [4]
w/dbenzene0.1420.464-0.588-3.099-4.6254.491 [1]
w/dtoluene0.1250.431-0.644-3.002-4.7484.524 [5]
w/dethylbenzene0.0930.467-0.723-3.001-4.8444.514 [5]
w/dfluorobenzene0.1390.152-0.374-3.030-4.6014.540 [1]
w/dchlorobenzene0.0650.381-0.521-3.183-4.7004.614 [1]
w/dbromobenzene-0.0170.436-0.424-3.174-4.5584.445 [1]
w/diodobenzene-0.1920.298-0.308-3.213-4.6534.588 [1]
w/dnitrobenzene-0.1960.5370.042-2.328-4.6084.314 [1]
wdiethyl ether0.2480.561-1.016-0.226-4.5534.075 [1]
wdiisopropyl ether0.4720.413-0.745-0.632-5.2514.059 [1]
wdibutyl ether0.2520.677-1.506-0.807-5.2494.815 [1]
wo-nitrophenyloctyl ether0.1210.600-0.459-2.246-3.8793.574 [1]
wethyl acetate0.4410.591-0.699-0.325-4.2613.666 [1]
wn-butyl acetate-0.4750.428-0.094-0.241-4.1514.046 [1]
wPGDP0.2560.501-0.828-1.022-4.6404.033 [1]
wmethyl isobutyl ketone0.3830.801-0.831-0.121-4.4413.876 [1]
w/dolive oil-0.0350.574-0.798-1.422-4.9844.210 [1]
w/dcarbon disulfide0.0470.686-0.943-3.603-5.8184.921 [1]
w/disopropyl myristate-0.6050.930-1.153-1.682-4.0934.249 [1]
w/dtriolein0.3850.983-2.083-2.007-3.4524.072 [1]
dmethanol0.2760.334-0.7140.243-3.323.549 [6]
dethanol/water(10:90)vol-0.173-0.023-0.0010.065-0.3720.454 [7]
dethanol/water(20:80)vol-0.2520.043-0.0400.096-0.8320.916 [7]
dethanol/water(30:70)vol-0.2690.107-0.0980.133-1.3161.414 [7]
dethanol/water(40:60)vol-0.2210.131-0.1590.171-1.8091.918 [7]
dethanol/water(50:50)vol-0.1420.124-0.2520.251-2.2752.415 [7]
dethanol/water(60:40)vol-0.040.138-0.3350.293-2.6752.812 [7]
dethanol/water(70:30)vol0.0630.085-0.3680.311-2.9363.102 [7]
dethanol/water(80:20)vol0.1720.175-0.4650.26-3.2123.323 [7]
dethanol/water(90:10)vol0.2430.213-0.5750.262-3.453.545 [7]
dethanol0.2220.471-1.0350.326-3.5963.857 [6]
d1-propanol0.1390.405-1.0290.247-3.7673.986 [6]
d1-butanol0.1650.401-1.0110.056-3.9584.044 [6]
d1-pentanol0.1500.536-1.2290.141-3.8644.077 [6]
d1-hexanol0.1150.492-1.1640.054-3.9784.131 [6]
d1-heptanol0.0350.398-1.0630.002-4.3424.317 [6]
d1-octanol-0.0340.489-1.044-0.024-4.2354.218 [1]
d1-decanol-0.0580.616-1.3190.026-4.1534.279 [6]
d2-propanol0.0990.343-1.0490.406-3.8274.033 [8]
d2-methyl-1-propanol0.1880.354-1.1270.016-3.5683.968 [8]
d2-butanol0.1270.253-0.9760.158-3.8824.114 [8]
d2-methyl-2-propanol0.2110.171-0.9470.331-4.0854.109 [8]
d3-methyl-1-butanol0.0730.36-1.2730.09-3.774.399 [8]
d2-pentanol0.1150.455-1.3310.206-3.7454.201 [1]
dethylene glycol-0.2430.695-0.6700.726-2.3992.670 [1]
dtrifluoroethanol0.395-0.094-0.594-1.280-1.2743.088 [1]
dTHF0.2230.363-0.384-0.238-4.9324.45 [9]
d1,4-dioxane0.1230.347-0.033-0.582-4.814.11 [9]
ddiethyl ether0.3500.358-0.820-0.588-4.9564.350 [10]
ddibutyl ether0.1760.394-0.985-1.414-5.3574.524 [10]
dmethyl t-butyl ether0.3410.307-0.817-0.618-5.0974.425 [10]
dmethyl acetate0.3510.223-0.150-1.035-4.5273.972 [1]
dethyl acetate0.3280.369-0.446-0.700-4.9044.150 [1]
dbutyl acetate0.2480.356-0.501-0.867-4.9734.281 [1]
dpropanone0.3130.312-0.121-0.608-4.7533.942 [1]
dbutanone0.2460.256-0.080-0.767-4.8554.148 [1]
dcyclohexanone0.0380.2250.058-0.976-4.8424.315 [1]
ddimethylformamide-0.305-0.0580.3430.358-4.8654.486 [1]
ddimethylacetamide-0.2710.0840.2090.915-5.0034.557 [1]
ddiethylacetamide0.2130.0340.0891.342-5.0844.088 [1]
ddibutylformamide0.3320.302-0.4360.358-4.9023.952 [1]
dN-methylpyrolidinone0.1470.5320.2250.840-4.7943.674 [1]
dN-methyl-2-piperidone0.0560.3320.2571.556-5.0353.983 [1]
dN-formylmorpholine-0.0320.696-0.0620.014-4.0923.405 [1]
dN-methylformamide0.1140.407-0.2870.542-4.0853.471 [1]
dN-ethylformamide0.2200.034-0.1660.935-4.5893.730 [1]
dN-methylacetamide0.0900.205-0.1721.305-4.5893.833 [1]
dN-ethylacetamide0.2840.128-0.4421.180-4.7283.856 [1]
dformamide-0.1710.0700.3080.589-3.1522.432 [1]
dacetonitrile0.4130.0770.326-1.566-4.3913.364 [1]
dbenzonitrile0.0970.2850.059-1.605-4.5624.028 [11]
dnitromethane0.023-0.0910.793-1.463-4.3643.460 [1]
dDMSO-0.1940.3270.7911.260-4.5403.361 [1]
dtributylphosphate0.3270.570-0.837-1.069-4.3333.919 [1]
dm-xylene0.1220.377-0.603-2.981-4.9614.535 [12]
do-xylene0.0830.518-0.813-2.884-4.8214.559 [12]
dp-xylene0.1660.477-0.812-2.939-4.8744.532 [12]
dsulfolane0.0000.1470.601-0.381-4.5413.29 [13]
n/agas–water-0.9940.5772.5493.8134.841-0.869 [1]
n/agas–water (37C)-1.0640.5882.5723.5914.341-0.971 [1]
n/agas–saline (37C)-1.2030.4862.4374.0314.316-0.745 [1]
wet/drysolventcesabvsource

Partition between gas phase and organic solvents

The LFER used to obtain partition coefficients that uses the systems below takes the form log Ks = c + eE + sS + aA + bB + lL

Coefficients for partition between given gas phase and solvent
wet/drysolventcesablsource
wButan-1-ol-0.0950.2621.3963.4052.5650.523 [1]
wPentan-1-ol-0.107-0.0011.1883.6141.6710.721 [1]
wHexan-1-ol-0.302-0.0460.8803.6091.7850.824 [1]
wHeptan-1-ol-0.1590.0180.8253.5391.4250.830 [1]
wOctan-1-ol-0.2220.0880.7013.4781.4770.851 [1]
wNonan-1-ol-0.1970.1410.6943.6161.2990.827 [1]
wDecan-1-ol-0.3020.2330.7413.5311.1770.835 [1]
wIsobutanol0.0000.0000.0000.0000.0000.000 [1]
w/dOleyl alcohol-0.268-0.3920.8003.1170.9780.918 [1]
w/dDichloromethane0.192-0.5721.4920.4600.8470.965 [1]
w/dTrichloromethane0.157-0.5601.2590.3741.3330.976 [1]
w/dTetrachloromethane0.217-0.4350.5540.0000.0001.069 [1]
w/d1,2-Dichloroethane0.017-0.3371.6000.7740.6370.921 [1]
w/d1-Chlorobutane0.130-0.5811.1140.7240.0001.016 [1]
w/dButane0.291-0.3600.0910.0000.0000.959 [1]
w/dPentane0.335-0.2760.0000.0000.0000.968 [1]
w/dHexane0.292-0.1690.0000.0000.0000.979 [1]
w/dHeptane0.275-0.1620.0000.0000.0000.983 [1]
w/dOctane0.215-0.0490.0000.0000.0000.967 [1]
w/dNonane0.200-0.1450.0000.0000.0000.980 [1]
w/dDecane0.156-0.1430.0000.0000.0000.989 [1]
w/dUndecane0.1130.0000.0000.0000.0000.971 [1]
w/dDodecane0.0530.0000.0000.0000.0000.986 [1]
w/dHexadecane0.0000.0000.0000.0000.0001.000 [1]
w/dCyclohexane0.163-0.1100.0000.0000.0001.013 [1]
w/dMethylcyclohexane0.318-0.2150.0000.0000.0001.012 [1]
w/dIsooctane0.264-0.2300.0000.0000.0000.975 [1]
w/dBenzene0.107-0.3131.0530.4570.1691.020 [1]
w/dToluene0.121-0.2220.9380.4670.0991.012 [1]
w/dFluorobenzene0.181-0.6211.4320.6470.0000.986 [1]
w/dChlorobenzene0.064-0.3991.1510.3130.1711.032 [1]
w/dBromobenzene-0.064-0.3261.2610.3230.2921.002 [1]
w/dIodobenzene-0.171-0.1921.1970.2450.2451.002 [1]
w/dNitrobenzene-0.2950.1211.6821.2470.3700.915 [1]
wDiethylether0.206-0.1690.8733.4020.0000.882 [1]
wDipropylether0.065-0.2020.7763.0740.0000.948 [1]
wDiisopropylether0.114-0.0320.6853.1080.0000.940 [1]
wDibutylether0.369-0.2160.0262.626-0.4991.124 [1]
wEthyl acetate0.1300.0311.2023.1990.4630.828 [1]
wn-Butyl acetate-0.6640.0611.6713.3730.8240.832 [1]
wMethyl isobutyl ketone0.2440.1830.9873.4180.3230.854 [1]
w/dOlive oil-0.159-0.2770.9041.695-0.0900.876 [1]
w/dCarbon disulfide0.1010.2510.1770.0270.0951.068 [1]
w/dTriolein0.1470.254-0.2461.5201.4730.918 [1]
dMethanol-0.004-0.2151.1733.7011.4320.769 [1]
dEthanol0.012-0.2060.7893.6351.3110.853 [1]
dPropan-1-ol-0.028-0.1850.6484.0221.0430.869 [1]
dButan-1-ol-0.039-0.2760.5393.7810.9950.934 [1]
dPentan-1-ol-0.042-0.2770.5263.7790.9830.932 [1]
dHexan-1-ol-0.035-0.2980.6263.7260.7290.936 [1]
dHeptan-1-ol-0.062-0.1680.4293.5411.1810.927 [1]
dOctan-1-ol-0.147-0.2140.5613.5070.7490.943 [1]
dDecan-1-ol-0.136-0.0680.3253.6740.7670.947 [1]
dPropan-2-ol-0.062-0.3270.7074.0241.0720.886 [1]
dIsobutanol0.012-0.4070.6703.6451.2830.895 [1]
ds-Butanol-0.017-0.3760.8523.7401.1610.867 [1]
dt-Butanol0.071-0.5380.8183.9510.8230.905 [1]
d3-Methylbutan-1-ol-0.014-0.3410.5253.6661.0960.925 [1]
d2-Pentanol-0.031-0.3250.4963.7921.0240.934 [1]
dEthylene glycol-0.8760.2781.4314.5842.5250.558 [1]
dTrifluoroethanol-0.092-0.5471.3392.2133.8070.645 [1]
dDiethylether0.288-0.3470.7752.9850.0000.973 [1]
dTHF0.189-0.3471.2383.2890.0000.982 [1]
dDioxane-0.034-0.3541.6743.0210.0000.919 [1]
dDibutylether0.165-0.4210.7602.102-0.6641.002 [1]
dMethyl t-butyl ether0.278-0.4890.8012.4950.0000.993 [1]
dMethyl acetate0.129-0.4471.6752.6250.2130.874 [1]
dEthyl acetate0.182-0.3521.3162.8910.0000.916 [1]
dn-Butyl acetate0.147-0.4141.2122.6230.0000.954 [1]
dPropanone0.127-0.3871.7333.0600.0000.866 [1]
dButanone0.112-0.4741.6712.8780.0000.916 [1]
dCyclohexanone-0.086-0.4411.7252.7860.0000.957 [1]
dDimethylformamide-0.391-0.8692.1073.7740.0001.011 [1]
dDimethylacetamide-0.308-0.7361.8024.3610.0001.028 [1]
dDiethylacetamide-0.075-0.4341.9114.8010.0000.899 [1]
dDibutylformamide-0.002-0.2391.4024.0290.0000.900 [1]
dN-Methylpyrrolidinone-0.128-0.0292.2174.4290.0000.777 [1]
dN-Methyl-2-piperidone-0.264-0.1712.0865.0560.0000.883 [1]
dN-Formylmorpholine-0.4370.0242.6314.3180.0000.712 [1]
dN-Methylformamide-0.249-0.1421.6614.1470.8170.739 [1]
dN-Ethylformamide-0.220-0.3021.7434.4980.4800.824 [1]
dN-Methylacetamide-0.197-0.1751.6084.8670.3750.837 [1]
dN-Ethylacetamide-0.018-0.1571.3524.5880.3570.824 [1]
dFormamide-0.8000.3102.2924.1301.9330.442 [1]
dAcetonitrile-0.007-0.5952.4612.0850.4180.738 [1]
dNitromethane-0.340-0.2972.6892.1930.5140.728 [1]
dDMSO-0.556-0.2232.9035.0360.0000.719 [1]
dTributylphosphate0.097-0.0981.1032.4110.5880.844 [1]
n/aGas–water-1.2710.8222.7433.9044.814-0.213 [1]
n/aGas–water (37C)-1.3470.9282.7953.7174.297-0.254 [1]
n/aGas–saline (37C)-1.4420.7652.6114.0844.316-0.194 [1]
wet/drysolventcesablsource
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Aqueous biphasic systems (ABS) or aqueous two-phase systems (ATPS) are clean alternatives for traditional organic-water solvent extraction systems.

Deep eutectic solvents or DESs are solutions of Lewis or Brønsted acids and bases which form a eutectic mixture. Deep eutectic solvents are highly tunable through varying the structure or relative ratio of parent components and thus have a wide variety of potential applications including catalytic, separation, and electrochemical processes. The parent components of deep eutectic solvents engage in a complex hydrogen bonding network which results in significant freezing point depression as compared to the parent compounds. The extent of freezing point depression observed in DESs is well illustrated by a mixture of choline chloride and urea in a 1:2 mole ratio. Choline chloride and urea are both solids at room temperature with melting points of 302 °C and 133 °C respectively, yet the combination of the two in a 1:2 molar ratio forms a liquid with a freezing point of 12 °C. DESs share similar properties to ionic liquids such as tunability and lack of flammability yet are distinct in that ionic liquids are neat salts composed exclusively of discrete ions. In contrast to ordinary solvents, such as Volatile Organic Compounds (VOC), DESs are non-flammable, and possess low vapour pressures and toxicity.

Implicit solvation is a method to represent solvent as a continuous medium instead of individual “explicit” solvent molecules, most often used in molecular dynamics simulations and in other applications of molecular mechanics. The method is often applied to estimate free energy of solute-solvent interactions in structural and chemical processes, such as folding or conformational transitions of proteins, DNA, RNA, and polysaccharides, association of biological macromolecules with ligands, or transport of drugs across biological membranes.

Micellar liquid chromatography (MLC) is a form of reversed phase liquid chromatography that uses an aqueous micellar solutions as the mobile phase.

Hydrophobicity scales are values that define the relative hydrophobicity or hydrophilicity of amino acid residues. The more positive the value, the more hydrophobic are the amino acids located in that region of the protein. These scales are commonly used to predict the transmembrane alpha-helices of membrane proteins. When consecutively measuring amino acids of a protein, changes in value indicate attraction of specific protein regions towards the hydrophobic region inside lipid bilayer.

Equilibrium chemistry is concerned with systems in chemical equilibrium. The unifying principle is that the free energy of a system at equilibrium is the minimum possible, so that the slope of the free energy with respect to the reaction coordinate is zero. This principle, applied to mixtures at equilibrium provides a definition of an equilibrium constant. Applications include acid–base, host–guest, metal–complex, solubility, partition, chromatography and redox equilibria.

MOSCED is a thermodynamic model for the estimation of limiting activity coefficients. From a historical point of view MOSCED can be regarded as an improved modification of the Hansen method and the Hildebrand solubility model by adding higher interaction term such as polarity, induction and separation of hydrogen bonding terms. This allows the prediction of polar and associative compounds, which most solubility parameter models have been found to do poorly. In addition to making quantitative prediction, MOSCED can be used to understand fundamental molecular level interaction for intuitive solvent selection and formulation.

In computational chemistry, a solvent model is a computational method that accounts for the behavior of solvated condensed phases. Solvent models enable simulations and thermodynamic calculations applicable to reactions and processes which take place in solution. These include biological, chemical and environmental processes. Such calculations can lead to new predictions about the physical processes occurring by improved understanding.

The n-octanol-water partition coefficient,Kow is a partition coefficient for the two-phase system consisting of n-octanol and water. Kow is also frequently referred to by the symbol P, especially in the English literature. It is also called n-octanol-water partition ratio.

References

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  3. Stephens TW et al. Correlation of solute partitioning into isooctane from water and from the gas phase based on updated Abraham equations. Global Journal of Physical Chemistry 2012, 3: 9
  4. 1 2 Abraham MH and Acree WE Jr. Linear free-energy relationships for water/hexadec-1-ene and water/deca-1,9-diene partitions, and for permeation through lipid bilayers; comparison of permeation systems. New J. Chem., 2012 doi : 10.1039/C2NJ40262A
  5. 1 2 Stephens TW et al. Correlation of Solute Transfer Into Toluene and Ethylbenzene from Water and from the Gas Phase Based on the Abraham Model. The Open Thermodynamics Journal, 2011, 5, 104-121
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  9. 1 2 Saifullah et al. Abraham Model Correlations for Transfer of Neutral Molecules to Tetrahydrofuran and to 1,4-Dioxane, and for Transfer of Ions to Tetrahydrofuran. Journal of Solution Chemistry. Volume 40, Number 12 (2011), 2082-2094, doi : 10.1007/s10953-011-9776-1
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  11. Abraham MH and Acree WE Jr. The transfer of neutral molecules, ions and ionic species from water to benzonitrile; comparison with nitrobenzene. Thermochimica Acta. Volume 526, Issues 1–2, 10 November 2011, Pages 22–28 doi : 10.1016/j.tca.2011.08.014
  12. 1 2 3 Stephens TW et al. Abraham model correlations for solute partitioning into o-xylene, m-xylene and p-xylene from both water and the gas phase. Fluid Phase Equilibria. Volume 308, Issues 1–2, 25 September 2011, Pages 64–71 doi : 10.1016/j.fluid.2011.06.010
  13. Stephens TW et al. Abraham model correlations for transfer of neutral molecules and ions to sulfolane. Fluid Phase Equilibria. Volume 309, Issue 1, 15 October 2011, Pages 30–35 doi : 10.1016/j.fluid.2011.06.037