| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6865 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -3131.30 ± 4.30 | kJ/mol | NIST |
| ΔfG° | -279.58 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -461.77 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | -551.00 ± 4.20 | kJ/mol | NIST |
| ΔfusH° | 12.24 | kJ/mol | Heat capacity measurement of organic thermal energy storage materials |
| ΔvapH° | 76.37 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.89 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.33 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.003 | Crippen Calculated Property | |
| McVol | 93.050 | ml/mol | McGowan Calculated Property |
| Pc | 4474.22 | kPa | Joback Calculated Property |
| Inp | 895.00 | NIST | |
| Tboil | [473.00; 478.95] | K |
|
| Tboil | 478.95 | K | Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation |
| Tboil | 475.65 ± 4.00 | K | NIST |
| Tboil | 473.00 ± 2.00 | K | NIST |
| Tc | 687.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tfus | [398.70; 403.00] | K |
|
| Tfus | 400.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 400.50 ± 1.50 | K | NIST |
| Tfus | 398.70 ± 2.00 | K | NIST |
| Tfus | 400.00 ± 3.00 | K | NIST |
| Tfus | 403.00 ± 1.50 | K | NIST |
| Tfus | 403.00 ± 3.00 | K | NIST |
| Tfus | 400.50 ± 1.50 | K | NIST |
| Ttriple | [314.95; 403.30] | K |
|
| Ttriple | 314.95 | K | Phase transition of neopentyl glycol in nanopores for thermal energy storage |
| Ttriple | 403.30 ± 0.10 | K | NIST |
| Ttriple | 403.30 ± 0.10 | K | NIST |
| Vc | 0.330 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.09; 316.09] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -1.55480e+01 | |||
| Coefficient B | 6.72640e-01 | |||
| Coefficient C | -4.80800e-04 | |||
| Coefficient D | 1.39800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 135.09 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 168.43 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 197.43 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 222.53 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 244.18 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 262.82 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 278.89 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 292.83 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 305.08 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 316.09 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008502; 0.0001333] | Pa×s | [400.84; 480.90] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.81992e+01 | |||
| Coefficient B | 4.46096e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 400.84 | |||
| Temperature range, max. | 480.90 | |||
| η | 0.0008502 | Pa×s | 400.84 | Calculated Property |
| η | 0.0006677 | Pa×s | 409.73 | Calculated Property |
| η | 0.0005298 | Pa×s | 418.63 | Calculated Property |
| η | 0.0004244 | Pa×s | 427.52 | Calculated Property |
| η | 0.0003431 | Pa×s | 436.42 | Calculated Property |
| η | 0.0002797 | Pa×s | 445.32 | Calculated Property |
| η | 0.0002299 | Pa×s | 454.21 | Calculated Property |
| η | 0.0001904 | Pa×s | 463.11 | Calculated Property |
| η | 0.0001588 | Pa×s | 472.00 | Calculated Property |
| η | 0.0001333 | Pa×s | 480.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.90; 4249.61] | kPa | [400.00; 643.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.32555e+02 | |||
| Coefficient B | -1.93531e+04 | |||
| Coefficient C | -3.09511e+01 | |||
| Coefficient D | 1.45892e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 400.00 | |||
| Temperature range, max. | 643.00 | |||
| Pvap | 2.90 | kPa | 400.00 | Calculated Property |
| Pvap | 11.33 | kPa | 427.00 | Calculated Property |
| Pvap | 35.60 | kPa | 454.00 | Calculated Property |
| Pvap | 94.20 | kPa | 481.00 | Calculated Property |
| Pvap | 217.70 | kPa | 508.00 | Calculated Property |
| Pvap | 452.06 | kPa | 535.00 | Calculated Property |
| Pvap | 862.60 | kPa | 562.00 | Calculated Property |
| Pvap | 1540.02 | kPa | 589.00 | Calculated Property |
| Pvap | 2610.10 | kPa | 616.00 | Calculated Property |
| Pvap | 4249.61 | kPa | 643.00 | Calculated Property |
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