| Literature DB >> 33267464 |
Hafiz Saqib Ali1,2, Jonathan Higham1,2, Richard H Henchman1,2.
Abstract
Accurately calculating the entropy of liquids is an important goal, given that many processes take place in the liquid phase. Of almost equal importance is understanding the values obtained. However, there are few methods that can calculate the entropy of such systems, and fewer still to make sense of the values obtained. We present our multiscale cell correlation (MCC) method to calculate the entropy of liquids from molecular dynamics simulations. The method uses forces and torques at the molecule and united-atom levels and probability distributions of molecular coordinations and conformations. The main differences with previous work are the consistent treatment of the mean-field cell approximation to the approriate degrees of freedom, the separation of the force and torque covariance matrices, and the inclusion of conformation correlation for molecules with multiple dihedrals. MCC is applied to a broader set of 56 important industrial liquids modeled using the Generalized AMBER Force Field (GAFF) and Optimized Potentials for Liquid Simulations (OPLS) force fields with 1.14*CM1A charges. Unsigned errors versus experimental entropies are 8.7 J K - 1 mol - 1 for GAFF and 9.8 J K - 1 mol - 1 for OPLS. This is significantly better than the 2-Phase Thermodynamics method for the subset of molecules in common, which is the only other method that has been applied to such systems. MCC makes clear why the entropy has the value it does by providing a decomposition in terms of translational and rotational vibrational entropy and topographical entropy at the molecular and united-atom levels.Entities:
Keywords: conformation; coordination; force; molecular dynamics simulation; probability distribution; structure; thermodynamics; torque
Year: 2019 PMID: 33267464 PMCID: PMC7515279 DOI: 10.3390/e21080750
Source DB: PubMed Journal: Entropy (Basel) ISSN: 1099-4300 Impact factor: 2.524
Boiling Temperature of Liquids [63] that are Gaseous at Ambient Conditions.
| Liquid | Liquid | Liquid | Liquid | ||||
|---|---|---|---|---|---|---|---|
| ammonia | 240 | ethane | 185 | hydrogen sulfide | 213 | methylamine | 267 |
| butane | 272 | ethene | 170 | methane | 112 | propane | 231 |
| carbon dioxide | 220 | ethylamine | 291 | methanethiol | 279 | TFE | 197 |
| diazene | 275 |
Pressure is 5.99 bar.
Figure 1Multiscale cell correlation (MCC) entropy values versus experiment for OPLS (blue), GAFF (red), and TraPPE (green), together with the line of perfect agreement (dotted).
Statistical Data for MCC and 2-Phase Thermodynamics (2PT) versus Experiment.
| Data Set (Number of Liquids) | Slope | Y-Intercept/J K |
| Zero-Intercept Slope | ||
|---|---|---|---|---|---|---|
| MCC OPLS | 9.8 | 0.6 | 0.94 | 11.7 | 0.95 | 1.00 |
| MCC GAFF (50) | 8.7 | −0.3 | 0.93 | 13.0 | 0.96 | 0.99 |
| 2PT OPLS | 15.5 | −15.6 | 1.05 | −25.3 | 0.84 | 0.92 |
| 2PT GAFF (14) | 28.0 | −24.4 | 0.97 | −19.5 | 0.55 | 0.87 |
| MCC OPLS | 4.9 | 2.3 | 0.87 | 26.7 | 0.89 | 1.01 |
| MCC GAFF (14) | 7.6 | 4.0 | 0.93 | 16.5 | 0.93 | 1.02 |
OPLS with 1.14*CM1A charges [52]; OPLS with charges optimised to liquid-phase properties [62].
Entropy by Experiment, MCC and 2PT (J K mol).
| Liquid | Experiment | MCC | 2PT [ | ||
|---|---|---|---|---|---|
| OPLS | GAFF | OPLS | GAFF | ||
| acetic acid | 158, 194 | 177 | 180 | 147 | 128 |
| acetone | 200 | 202 | 206 | 198 | 187 |
| acetonitrile | 150 | 143 | 145 | ||
| ammonia | 87 | 71 | 92 | ||
| aniline | 191, 192 | 205 | 205 | ||
| benzene | 173, 175 | 183 | 182 | 172 | 161 |
| benzyl alcohol | 217 | 216 | 208 | ||
| benzaldehyde | 221 | 204 | 204 | ||
| butane | 227, 230, 231 | 214 | 212 | ||
| butanol | 226, 228 | 244 | 235 | ||
| 2-butoxyethanol | 293 | 301 | |||
| carbon dioxide | 118 | 111 | 106 | 112 | |
| chloroform | 202 e | 203 | 210 | 193 | 226 |
| cyclohexane | 204, 206 | 220 | 212 | ||
| diazene | 121 | 125 | 116 | ||
| dichloromethane | 175 | 190 | 191 | ||
| diethanolamine | 248 | 256 | |||
| diethyl ether | 253, 254 | 237 | 236 | ||
| DMFA | 214 | 222 | |||
| DMSO | 189 | 183 | 202 | 164 | 159 |
| 1,4-dioxane | 197 | 206 | 199 | 179 | 159 |
| ethane | 127 | 125 | 127 | ||
| ethanol | 160, 161, 177 | 177 | 175 | 141 | 127 |
| ethene | 118 | 114 | 120 | ||
| ethyl acetate | 259 | 254 | 252 | ||
| ethylamine | 189 | 181 | 185 | ||
| ethylene glycol | 167, 180 | 172 | 175 | 141 | 121 |
| formamide | 151 | 153 | |||
| formic acid | 128, 132, 143 | 156 | 145 | ||
| furan | 177 | 181 | 186 | 167 | 157 |
| hexane | 290, 295, 296 | 273 | 272 | 251 | |
| hexanol | 287 | 288 | 281 | ||
| hydrazine | 122 | 120 | 116 | ||
| hydrogen peroxide | 110 | 126 | 125 | ||
| hydrogen sulfide | 106 | 101 | |||
| methane | 79 | 73 | 78 | ||
| methanethiol | 163 | 177 | 172 | ||
| methanol | 127, 130, 136 | 139 | 139 | 117 | 109 |
| methylamine | 150 | 128 | 133 | ||
| NMA | 205 | 206 | 181 | 168 | |
| octanol | 335 | 331 | |||
| pentane | 259, 263 | 251 | 250 | ||
| pentanol | 255, 259 | 264 | 257 | ||
| piperidine | 210 | 234 | 222 | ||
| propane | 171 | 176 | 176 | ||
| propanol | 193, 214 | 213 | 206 | ||
| pyridine | 178, 179, 210 | 191 | 189 | ||
| styrene | 238, 241 | 223 | 223 | ||
| TBA | 190, 198 | 218 | 217 | ||
| tetrahydrofuran | 204 | 188 | 192 | 196 | 159 |
| TFE | 184 | 207 | 195 | 185 | |
| toluene | 219, 221 | 224 | 223 | 204 | 190 |
| triethylamine | 309 | 292 | 295 | ||
| m-xylene | 252, 254 | 248 | 248 | ||
| o-xylene | 246, 248 | 245 | 245 | ||
| p-xylene | 244, 247, 253 | 243 | 243 | ||
Reference [63] Experimental errors J K mol ; Reference [64]; References [50,69]; TraPPE force field [58]; Reference [65]; Derived in Table S2 using References [63,70]; Reference [51]; Reference [67]; Reference [68]; Reference [66].
Figure 2MCC entropy components for GAFF (bottom to top): molecular-translational (dark blue), molecular rotational (blue), molecular topographical (cyan), united-atom translational (dark red) united-atom rotational (red), and united-atom topographical (orange).
Figure 3MCC entropy components for GAFF versus molecular mass for all liquids. The colouring is as in Figure 2.
Lines of Best Fit for the Entropy Components versus Molecular Mass.
| Component | Slope/J K | Y-Intercept/J K |
| Component | Slope/J K | Y-Intercept/J K |
|
|---|---|---|---|---|---|---|---|
|
| 0.21 | 50 | 0.54 |
| 0.42 | 14 | 0.63 |
|
| 0.35 | 28 | 0.70 |
| 0.43 | 6 | 0.34 |
|
| 0.09 | 16 | 0.13 |
| 0.39 | 16 | 0.87 |
Figure 4Panels for five representative liquids (GAFF) illustrating the UA force (left) and torque (right) covariance matrices and coordination-number probability distributions (lower). For the matrices, white and black represent correlations of 1 and −1, respectively, with grey in between. The matrix origin is at the lower left.