- InChI
- InChI=1S/C5H5N/c1-2-4-6-5-3-1/h1-5H
- InChI Key
- JUJWROOIHBZHMG-UHFFFAOYSA-N
- Formula
- C5H5N
- SMILES
- c1ccncc1
- Molecular Weight1
- 79.10
- CAS
- 110-86-1
- Other Names
-
- Azabenzene
- CP 32
- NCI-C55301
- NSC 406123
- Piridina
- Pirydyna
- Pyr
- Pyridin
- Rcra waste number U196
- UN 1282
- azine
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- SProt : Protonation entropy at 298K (J/mol×K).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2430 | KDB | |
| PAff | [930.00; 936.50] | kJ/mol |
|
| PAff | 930.00 | kJ/mol | NIST |
| PAff | 936.50 ± 8.50 | kJ/mol | NIST |
| Tig | 755.37 | K | KDB |
| BasG | 898.10 | kJ/mol | NIST |
| ΔcH°liquid | [-2782.40; -2725.00] | kJ/mol |
|
| ΔcH°liquid | -2725.00 | kJ/mol | NIST |
| ΔcH°liquid | -2782.20 ± 0.42 | kJ/mol | NIST |
| ΔcH°liquid | -2782.40 ± 1.50 | kJ/mol | NIST |
| ΔcH°liquid | -2758.00 | kJ/mol | NIST |
| μ | 2.30 | debye | KDB |
| SProt | -1.00 ± 10.00 | J/mol×K | NIST |
| LFL | 1.80 | % in Air | KDB |
| UFL | 12.40 | % in Air | KDB |
| Tflash,oc | 293.15 | K | KDB |
| ΔfG° | 190.30 | kJ/mol | KDB |
| Rg | 3.0500 | KDB | |
| ΔfH°gas | [110.10; 140.70] | kJ/mol |
|
| ΔfH°gas | 140.30 | kJ/mol | KDB |
| ΔfH°gas | 140.20 | kJ/mol | NIST |
| ΔfH°gas | 140.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | 140.70 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | 110.10 | kJ/mol | NIST |
| ΔfH°liquid | [69.90; 100.20] | kJ/mol |
|
| ΔfH°liquid | 99.96 ± 0.50 | kJ/mol | NIST |
| ΔfH°liquid | 100.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | 69.90 | kJ/mol | NIST |
| ΔvapH° | [35.50; 40.50] | kJ/mol |
|
| ΔvapH° | 40.21 | kJ/mol | NIST |
| ΔvapH° | 40.50 ± 1.10 | kJ/mol | NIST |
| ΔvapH° | 40.16 ± 0.06 | kJ/mol | NIST |
| ΔvapH° | 40.40 | kJ/mol | NIST |
| ΔvapH° | 40.15 | kJ/mol | NIST |
| ΔvapH° | 40.20 | kJ/mol | NIST |
| ΔvapH° | 40.20 | kJ/mol | NIST |
| ΔvapH° | 40.40 | kJ/mol | NIST |
| ΔvapH° | 40.20 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 40.50 | kJ/mol | NIST |
| ΔvapH° | Outlier 35.50 ± 0.04 | kJ/mol | NIST |
| IE | [9.10; 9.90] | eV |
|
| IE | 9.26 ± 0.01 | eV | NIST |
| IE | 9.34 ± 0.03 | eV | NIST |
| IE | 9.25 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.25 | eV | NIST |
| IE | 9.74 ± 0.05 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | Outlier 9.90 ± 0.10 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.66 ± 0.03 | eV | NIST |
| IE | 9.70 ± 0.05 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.30 ± 0.01 | eV | NIST |
| IE | 9.10 | eV | NIST |
| IE | 9.10 ± 0.01 | eV | NIST |
| IE | 9.31 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.20 ± 0.05 | eV | NIST |
| IE | 9.40 | eV | NIST |
| IE | 9.27 | eV | NIST |
| IE | 9.23 ± 0.03 | eV | NIST |
| IE | 9.80 ± 0.20 | eV | NIST |
| IE | 9.51 | eV | NIST |
| IE | 9.66 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.60 ± 0.50 | eV | NIST |
| IE | 9.59 | eV | NIST |
| log10WS | [0.76; 0.76] |
|
|
| log10WS | 0.76 | Aq. Solubility Prediction | |
| log10WS | 0.76 | Estimated Solubility | |
| logPoct/wat | 1.082 | Crippen Calculated Property | |
| McVol | 67.530 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [5640.00; 6079.50] | kPa |
|
| Pc | 5670.00 | kPa | KDB |
| Pc | 5660.00 ± 5.65 | kPa | NIST |
| Pc | 5640.00 ± 103.40 | kPa | NIST |
| Pc | 6079.50 ± 81.06 | kPa | NIST |
| Inp | [104.40; 772.00] |
|
|
| Inp | 736.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 724.40 | NIST | |
| Inp | 727.87 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 723.40 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 737.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 721.60 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 705.90 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 731.50 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 735.60 | NIST | |
| Inp | 736.70 | NIST | |
| Inp | 739.10 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 715.50 | NIST | |
| Inp | 735.60 | NIST | |
| Inp | 736.70 | NIST | |
| Inp | 739.10 | NIST | |
| Inp | 737.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 752.50 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | Outlier 104.40 | NIST | |
| Inp | Outlier 108.15 | NIST | |
| Inp | Outlier 121.47 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 736.70 | NIST | |
| Inp | 731.00 | NIST | |
| I | [1156.00; 1233.00] |
|
|
| I | 1218.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1216.00 | NIST | |
| I | Outlier 1224.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1185.00 | NIST | |
| I | Outlier 1233.00 | NIST | |
| I | Outlier 1227.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1190.10 | NIST | |
| I | 1196.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1194.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1209.00 | NIST | |
| I | 1209.00 | NIST | |
| I | 1211.00 | NIST | |
| I | 1182.74 | NIST | |
| I | 1218.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1199.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1199.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1209.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1190.00 | NIST | |
| I | Outlier 1156.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1193.00 | NIST | |
| I | Outlier 1220.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1159.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1209.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1198.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1180.00 | NIST | |
| I | Outlier 1157.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1174.00 | NIST | |
| I | Outlier 1224.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1181.00 | NIST | |
| S°liquid | [177.90; 210.41] | J/mol×K |
|
| S°liquid | 177.90 | J/mol×K | NIST |
| S°liquid | 179.10 | J/mol×K | NIST |
| S°liquid | 210.41 | J/mol×K | NIST |
| Tboil | [386.00; 390.65] | K |
|
| Tboil | 389.00 | K | Effect of Dissolved Inorganic Salts on the Enthalpy of Mixing of the Ethanol + Pyridine System at 303.15 K |
| Tboil | 387.90 | K | Effect of Cadmium Chloride and Ammonium Chloride Salts on the Enthalpy of Mixing of the Pyridine + Water at 303.15 K |
| Tboil | 388.38 | K | KDB |
| Tboil | 389.15 ± 0.50 | K | NIST |
| Tboil | 388.70 | K | NIST |
| Tboil | 388.15 ± 1.00 | K | NIST |
| Tboil | 388.40 | K | NIST |
| Tboil | 388.55 ± 0.50 | K | NIST |
| Tboil | 388.40 ± 0.20 | K | NIST |
| Tboil | 388.75 ± 0.10 | K | NIST |
| Tboil | 388.70 ± 0.10 | K | NIST |
| Tboil | 388.55 ± 0.25 | K | NIST |
| Tboil | 388.77 ± 0.30 | K | NIST |
| Tboil | 388.75 ± 0.30 | K | NIST |
| Tboil | 388.70 ± 0.30 | K | NIST |
| Tboil | 388.35 ± 0.40 | K | NIST |
| Tboil | 388.27 ± 0.20 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 388.70 ± 0.20 | K | NIST |
| Tboil | 388.00 ± 3.00 | K | NIST |
| Tboil | 388.55 ± 0.30 | K | NIST |
| Tboil | 389.05 ± 0.40 | K | NIST |
| Tboil | 388.35 ± 0.30 | K | NIST |
| Tboil | 388.46 ± 0.13 | K | NIST |
| Tboil | 388.75 ± 0.30 | K | NIST |
| Tboil | 388.55 ± 0.20 | K | NIST |
| Tboil | 388.35 ± 0.25 | K | NIST |
| Tboil | 388.41 | K | NIST |
| Tboil | 388.40 ± 0.15 | K | NIST |
| Tboil | 388.40 ± 0.20 | K | NIST |
| Tboil | 388.50 ± 0.15 | K | NIST |
| Tboil | 388.00 ± 0.25 | K | NIST |
| Tboil | 388.45 ± 0.50 | K | NIST |
| Tboil | 388.15 ± 1.50 | K | NIST |
| Tboil | 388.20 ± 0.50 | K | NIST |
| Tboil | 388.60 ± 0.15 | K | NIST |
| Tboil | 388.39 ± 0.15 | K | NIST |
| Tboil | 389.00 ± 0.10 | K | NIST |
| Tboil | 388.45 ± 0.20 | K | NIST |
| Tboil | 388.40 ± 0.10 | K | NIST |
| Tboil | 388.39 ± 0.20 | K | NIST |
| Tboil | 388.39 ± 0.20 | K | NIST |
| Tboil | 388.35 ± 0.15 | K | NIST |
| Tboil | 388.45 ± 0.50 | K | NIST |
| Tboil | 388.31 ± 0.10 | K | NIST |
| Tboil | 388.55 ± 0.30 | K | NIST |
| Tboil | 388.80 ± 0.20 | K | NIST |
| Tboil | 387.70 ± 0.50 | K | NIST |
| Tboil | 388.68 ± 0.20 | K | NIST |
| Tboil | 387.63 ± 0.20 | K | NIST |
| Tboil | 388.40 ± 0.50 | K | NIST |
| Tboil | 388.25 ± 0.30 | K | NIST |
| Tboil | Outlier 386.00 ± 1.50 | K | NIST |
| Tboil | 388.60 ± 0.50 | K | NIST |
| Tboil | 388.55 ± 0.50 | K | NIST |
| Tboil | 388.55 ± 0.20 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 388.15 ± 1.50 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 388.15 ± 0.20 | K | NIST |
| Tboil | 388.55 ± 0.30 | K | NIST |
| Tboil | 389.25 ± 0.40 | K | NIST |
| Tboil | 388.45 ± 0.40 | K | NIST |
| Tboil | 388.45 ± 0.40 | K | NIST |
| Tboil | 388.20 ± 0.50 | K | NIST |
| Tboil | 388.50 ± 0.30 | K | NIST |
| Tboil | 387.65 ± 1.50 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 389.20 ± 0.30 | K | NIST |
| Tboil | 388.50 ± 0.30 | K | NIST |
| Tboil | Outlier 390.65 ± 0.70 | K | NIST |
| Tboil | 388.65 ± 0.40 | K | NIST |
| Tboil | 388.70 ± 0.30 | K | NIST |
| Tboil | 388.65 ± 0.50 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 388.65 ± 0.35 | K | NIST |
| Tboil | 389.00 ± 0.50 | K | NIST |
| Tboil | 388.15 ± 1.00 | K | NIST |
| Tboil | 388.50 ± 0.20 | K | NIST |
| Tboil | 388.30 ± 0.30 | K | NIST |
| Tboil | 388.45 ± 0.30 | K | NIST |
| Tboil | 388.35 ± 0.25 | K | NIST |
| Tboil | 388.66 ± 0.40 | K | NIST |
| Tboil | Outlier 389.60 ± 1.00 | K | NIST |
| Tboil | Outlier 389.60 ± 1.00 | K | NIST |
| Tboil | 387.65 ± 1.50 | K | NIST |
| Tc | [617.75; 620.20] | K |
|
| Tc | 620.00 | K | KDB |
| Tc | 620.20 ± 0.61 | K | NIST |
| Tc | 620.00 | K | NIST |
| Tc | 619.95 ± 0.20 | K | NIST |
| Tc | 618.15 ± 0.40 | K | NIST |
| Tc | 620.00 ± 2.00 | K | NIST |
| Tc | 618.00 ± 0.35 | K | NIST |
| Tc | 617.75 ± 0.35 | K | NIST |
| Tc | 618.15 ± 0.40 | K | NIST |
| Tc | 620.15 ± 6.00 | K | NIST |
| Tfus | [231.00; 235.65] | K |
|
| Tfus | 231.49 | K | KDB |
| Tfus | 231.25 | K | Aq. Solubility Prediction |
| Tfus | 231.42 ± 0.08 | K | NIST |
| Tfus | 231.44 ± 0.05 | K | NIST |
| Tfus | 231.15 ± 0.50 | K | NIST |
| Tfus | 231.15 ± 0.10 | K | NIST |
| Tfus | 231.15 ± 4.00 | K | NIST |
| Tfus | 231.60 ± 0.06 | K | NIST |
| Tfus | 231.31 ± 0.20 | K | NIST |
| Tfus | 231.55 ± 0.15 | K | NIST |
| Tfus | 231.40 ± 0.20 | K | NIST |
| Tfus | 231.65 ± 0.30 | K | NIST |
| Tfus | 231.35 ± 0.40 | K | NIST |
| Tfus | 231.20 ± 0.20 | K | NIST |
| Tfus | 231.15 ± 0.20 | K | NIST |
| Tfus | 233.65 ± 0.70 | K | NIST |
| Tfus | 231.40 ± 0.30 | K | NIST |
| Tfus | 233.75 ± 1.50 | K | NIST |
| Tfus | Outlier 235.65 ± 0.30 | K | NIST |
| Tfus | 232.45 ± 0.20 | K | NIST |
| Tfus | 231.15 ± 0.30 | K | NIST |
| Tfus | 231.15 ± 0.40 | K | NIST |
| Tfus | 233.15 ± 1.00 | K | NIST |
| Tfus | 231.35 ± 0.40 | K | NIST |
| Tfus | Outlier 235.15 ± 0.50 | K | NIST |
| Tfus | 231.00 ± 2.00 | K | NIST |
| Tfus | 231.20 ± 0.40 | K | NIST |
| Tfus | 231.15 ± 0.40 | K | NIST |
| Ttriple | [231.48; 231.48] | K |
|
| Ttriple | 231.48 | K | KDB |
| Ttriple | 231.48 ± 0.03 | K | NIST |
| Ttriple | 231.48 ± 0.05 | K | NIST |
| Ttriple | 231.48 ± 0.05 | K | NIST |
| Vc | [0.243; 0.253] | m3/kmol |
|
| Vc | 0.243 | m3/kmol | KDB |
| Vc | 0.253 ± 0.005 | m3/kmol | NIST |
| Zc | 0.2672770 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 2130.00 | 979.0 |
| 298.15 | 4150.00 | 980.4 |
| 298.15 | 6180.00 | 981.8 |
| 298.15 | 8210.00 | 983.2 |
| 298.15 | 10230.00 | 984.5 |
| 298.15 | 11250.00 | 985.1 |
| 298.15 | 12260.00 | 985.8 |
| 298.15 | 14290.00 | 987.1 |
| 298.15 | 16310.00 | 988.3 |
| 298.15 | 18340.00 | 989.6 |
| 298.15 | 20370.00 | 990.8 |
| 298.15 | 22390.00 | 992.1 |
| 298.15 | 24420.00 | 993.3 |
| 298.15 | 26450.00 | 994.5 |
| 298.15 | 28470.00 | 995.7 |
| 298.15 | 29490.00 | 996.3 |
| 298.15 | 30500.00 | 996.9 |
| 298.15 | 32530.00 | 998.0 |
| 298.15 | 34550.00 | 999.1 |
| 298.15 | 36580.00 | 1000.3 |
| 298.15 | 38600.00 | 1001.4 |
| 298.15 | 39620.00 | 1002.0 |
| 308.15 | 2130.00 | 969.2 |
| 308.15 | 4150.00 | 970.6 |
| 308.15 | 6180.00 | 972.1 |
| 308.15 | 8210.00 | 973.5 |
| 308.15 | 10230.00 | 974.9 |
| 308.15 | 11250.00 | 975.6 |
| 308.15 | 12260.00 | 976.3 |
| 308.15 | 14290.00 | 977.6 |
| 308.15 | 16310.00 | 978.9 |
| 308.15 | 18340.00 | 980.3 |
| 308.15 | 20370.00 | 981.6 |
| 308.15 | 22390.00 | 982.8 |
| 308.15 | 24420.00 | 984.1 |
| 308.15 | 26450.00 | 985.4 |
| 308.15 | 28470.00 | 986.7 |
| 308.15 | 29490.00 | 987.2 |
| 308.15 | 30500.00 | 987.8 |
| 308.15 | 32530.00 | 989.0 |
| 308.15 | 34550.00 | 990.3 |
| 308.15 | 36580.00 | 991.5 |
| 308.15 | 38600.00 | 992.6 |
| 308.15 | 39620.00 | 993.2 |
| 318.15 | 2130.00 | 959.3 |
| 318.15 | 4150.00 | 960.8 |
| 318.15 | 6180.00 | 962.3 |
| 318.15 | 8210.00 | 963.7 |
| 318.15 | 10230.00 | 965.2 |
| 318.15 | 11250.00 | 966.0 |
| 318.15 | 12260.00 | 966.7 |
| 318.15 | 14290.00 | 968.1 |
| 318.15 | 16310.00 | 969.5 |
| 318.15 | 18340.00 | 970.9 |
| 318.15 | 20370.00 | 972.2 |
| 318.15 | 22390.00 | 973.6 |
| 318.15 | 24420.00 | 974.9 |
| 318.15 | 26450.00 | 976.2 |
| 318.15 | 28470.00 | 977.6 |
| 318.15 | 29490.00 | 978.2 |
| 318.15 | 30500.00 | 978.8 |
| 318.15 | 32530.00 | 980.1 |
| 318.15 | 34550.00 | 981.4 |
| 318.15 | 36580.00 | 982.6 |
| 318.15 | 38600.00 | 983.8 |
| 318.15 | 39620.00 | 984.4 |
| 328.15 | 2130.00 | 949.2 |
| 328.15 | 4150.00 | 950.7 |
| 328.15 | 6180.00 | 952.3 |
| 328.15 | 8210.00 | 953.9 |
| 328.15 | 10230.00 | 955.4 |
| 328.15 | 11250.00 | 956.2 |
| 328.15 | 12260.00 | 956.9 |
| 328.15 | 14290.00 | 958.4 |
| 328.15 | 16310.00 | 959.9 |
| 328.15 | 18340.00 | 961.3 |
| 328.15 | 20370.00 | 962.8 |
| 328.15 | 22390.00 | 964.2 |
| 328.15 | 24420.00 | 965.6 |
| 328.15 | 26450.00 | 967.0 |
| 328.15 | 28470.00 | 968.3 |
| 328.15 | 29490.00 | 969.0 |
| 328.15 | 30500.00 | 969.7 |
| 328.15 | 32530.00 | 971.0 |
| 328.15 | 34550.00 | 972.3 |
| 328.15 | 36580.00 | 973.6 |
| 328.15 | 38600.00 | 975.0 |
| 328.15 | 39620.00 | 975.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 978.25 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [285.10; 414.07] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45260e+01 | |||
| Coefficient B | -3.36808e+03 | |||
| Coefficient C | -4.85520e+01 | |||
| Temperature range, min. | 285.10 | |||
| Temperature range, max. | 414.07 | |||
| Pvap | 1.33 | kPa | 285.10 | Calculated Property |
| Pvap | 3.01 | kPa | 299.43 | Calculated Property |
| Pvap | 6.21 | kPa | 313.76 | Calculated Property |
| Pvap | 11.91 | kPa | 328.09 | Calculated Property |
| Pvap | 21.43 | kPa | 342.42 | Calculated Property |
| Pvap | 36.51 | kPa | 356.75 | Calculated Property |
| Pvap | 59.34 | kPa | 371.08 | Calculated Property |
| Pvap | 92.52 | kPa | 385.41 | Calculated Property |
| Pvap | 139.13 | kPa | 399.74 | Calculated Property |
| Pvap | 202.64 | kPa | 414.07 | Calculated Property |
| Pvap | [0.02; 5646.24] | kPa | [231.51; 619.95] |
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 | 7.55215e+01 | |||
| Coefficient B | -7.22139e+03 | |||
| Coefficient C | -8.90767e+00 | |||
| Coefficient D | 5.30428e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 231.51 | |||
| Temperature range, max. | 619.95 | |||
| Pvap | 0.02 | kPa | 231.51 | Calculated Property |
| Pvap | 0.68 | kPa | 274.67 | Calculated Property |
| Pvap | 7.50 | kPa | 317.83 | Calculated Property |
| Pvap | 42.62 | kPa | 360.99 | Calculated Property |
| Pvap | 157.26 | kPa | 404.15 | Calculated Property |
| Pvap | 434.01 | kPa | 447.31 | Calculated Property |
| Pvap | 980.33 | kPa | 490.47 | Calculated Property |
| Pvap | 1923.51 | kPa | 533.63 | Calculated Property |
| Pvap | 3415.00 | kPa | 576.79 | Calculated Property |
| Pvap | 5646.24 | kPa | 619.95 | Calculated Property |
| Pvap | [19.94; 270.13] | kPa | [340.50; 426.04] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41902e+01 | |||
| Coefficient B | -3.15767e+03 | |||
| Coefficient C | -5.84960e+01 | |||
| Reference | McCullough, Douslin, et al., 1957 | |||
| Temperature range, min. | 340.50 | |||
| Temperature range, max. | 426.04 | |||
| Pvap | 19.94 | kPa | 340.50 | Calculated Property |
| Pvap | 28.73 | kPa | 350.00 | Calculated Property |
| Pvap | 40.45 | kPa | 359.51 | Calculated Property |
| Pvap | 55.76 | kPa | 369.01 | Calculated Property |
| Pvap | 75.43 | kPa | 378.52 | Calculated Property |
| Pvap | 100.26 | kPa | 388.02 | Calculated Property |
| Pvap | 131.15 | kPa | 397.53 | Calculated Property |
| Pvap | 169.08 | kPa | 407.03 | Calculated Property |
| Pvap | 215.05 | kPa | 416.54 | Calculated Property |
| Pvap | 270.13 | kPa | 426.04 | Calculated Property |
| Pvap | [19.94; 270.13] | kPa | [340.50; 426.04] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41902e+01 | |||
| Coefficient B | -3.15767e+03 | |||
| Coefficient C | -5.84960e+01 | |||
| Reference | McCullough, Douslin, et al., 1957, 2 | |||
| Temperature range, min. | 340.50 | |||
| Temperature range, max. | 426.04 | |||
| Pvap | 19.94 | kPa | 340.50 | Calculated Property |
| Pvap | 28.73 | kPa | 350.00 | Calculated Property |
| Pvap | 40.45 | kPa | 359.51 | Calculated Property |
| Pvap | 55.76 | kPa | 369.01 | Calculated Property |
| Pvap | 75.43 | kPa | 378.52 | Calculated Property |
| Pvap | 100.26 | kPa | 388.02 | Calculated Property |
| Pvap | 131.15 | kPa | 397.53 | Calculated Property |
| Pvap | 169.08 | kPa | 407.03 | Calculated Property |
| Pvap | 215.05 | kPa | 416.54 | Calculated Property |
| Pvap | 270.13 | kPa | 426.04 | Calculated Property |
Similar Compounds
Find more compounds similar to Pyridine.
Mixtures
- 1,2-Ethanediol + Pyridine + TETRAMETHYLAMMONIUM CHLORIDE
- Toluene + Pyridine
- Tetrahydropyran + Pyridine + BENZENAMINE, 2-METHYL-
- Pyridine + TETRAMETHYLAMMONIUM CHLORIDE + Glycerin
- Pyridine + Heptane
- Pyridine + Octane
- Pyridine + Nonane
- Pyridine + Decane
- Undecane + Pyridine
- 1-Heptene + Pyridine
- 1-Heptyne + Pyridine
- Pyridine + Benzene, ethyl-
- Pyridine + o-Xylene
- Pyridine + Benzene, 1,3-dimethyl-
- p-Xylene + Pyridine
- Acetonitrile + Pyridine
- Pyridine + Acetic acid, butyl ester
- Pyridine + Butane, 1-chloro-
- Propane, 1,2-dichloro- + Pyridine
- Propane, 2-bromo- + Pyridine
Find more mixtures with Pyridine.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Association in Dilute Aqueous Solution of Pyridine and Its Methyl Derivatives Studied by Cryoscopic Method
- Temperature dependences of limiting activity coefficients and Henry s law constants for N-methylpyrrolidone, pyridine, and piperidine in water
- Thermodynamic properties of aqueous solutions of pyridine and piperidine
- Ionic liquids on desulfurization of fuel oils
- Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
- Liquid liquid equilibria of imidazolium based ionic liquid + pyridine + hydrocarbon at 298.15 K: Experiments and correlations
- Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
- Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
- Phase diagrams of binary systems containing tricyanomethanide-based ionic liquids and thiophene or pyridine - new experimental data and PC-SAFT modeling
- Extraction of aromatic nitrogen compounds from heptane quinolinium and isoquinolinium based ionic liquids
- Extraction of nitrogen compounds from diesel fuel using imidazolium- and pyridinium- based ionic liquids: Experiments, COSMO-RS prediction and NRTL correlation
- Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Densities, viscosities and refractive indices of binary mixtures containing methyl ethyl ketone. Friction theory. New UNIFAC-VISCO and ASOG-VISCO parameter determination
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Separation of the mixture pyridine + methylbenzene via several acidic ionic liquids: Phase equilibrium measurement and correlation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Volumetric properties of pyridine, 2-picoline, 3-picoline, and 4-picoline at temperatures from (298.15 to 328.15) K and at pressures up to 40 MPa
- Thermodynamic studies of molecular interactions in mixtures of o-toulidine with pyridine and picolines: Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
- Topological investigations of binary mixtures containing ionic liquid 1-ethyl-3-methylimidazolium tetrafluoroborate and pyridine or isomeric picolines
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Quaternary (liquid +liquid) equilibria for systems of imidazolium based ionic liquid + thiophene + pyridine + cyclohexane at 298.15 K: Experiments and quantum chemical predictions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Excess molar enthalpies for [emim][BF4] + pyrrolidin-2-one or 1-methyl pyrrolidin-2-one + pyridine or water mixtures
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
- Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Excess heat capacities of (binary + ternary) mixtures containing [emim][BF4] and organic liquids
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Effect of organic solvents on lowering the viscosity of 1-hexyl-3- methylimidazolium chloride
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermochemistry of adducts of some bivalent transition metal bromides with pyridine
- Adducts of antimony tri-iodide and aromatic amines: A calorimetric study
- Effect of electrostatic interaction on thermochemical behavior of 12-crown-4 ether in various polar solvents
- Thermodynamic properties of binary mixtures of tetrahydropyran with pyridine and isomeric picolines: Excess molar volumes, excess molar enthalpies and excess isentropic compressibilities
- Excess molar enthalpies of ternary mixtures containing o-toluidine + tetrahydropyran with pyridine or isomeric picolines or benzene or toluene at 308.15K
- Thermodynamic functions of hydrogen bonding of amines in methanol: head space analysis and solution calorimetry
- Excess heat capacities of 1-methyl pyrrolidin-2-one and pyridine orpicolines mixtures
- Excess molar enthalpies of ternary mixtures containing1-ethyl-3-methylimidazolium tetrafluoroborate and organic solvents
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
- Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
- Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
- Thermochemistry of hydrogen bonding of linear and cyclic amides inproton acceptors media
- Thermochemistry of hydrogen bonding of proton acceptors in the media of linear and cyclic amides. Cooperativity effects in multi-particle complexes of amides
- Analysis of solute-pyridine intermolecular interactions based on experimental enthalpies of solution and enthalpies of solvation of solutes dissolved in pyridine
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
- Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
- Influence of Aprotic Cosolvents on the Thermophysical Properties of Imidazolium-Based Ionic Liquid
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Extraction Ability of Nitrogen-Containing Compounds Involved in the Desulfurization of Fuels by Using Ionic Liquids
- Effect of Dissolved Inorganic Salts on the Enthalpy of Mixing of the Ethanol + Pyridine System at 303.15 K
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
- Mixtures of Pyridine and Nicotine with Pyridinium-Based Ionic Liquids
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Effect of Cadmium Chloride and Ammonium Chloride Salts on the Enthalpy of Mixing of the Pyridine + Water at 303.15 K
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquids and Organic Solvents
- Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
- Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
- Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
- (Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 298.15 K
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Thermodynamics of Ketone + Amine Mixtures. I. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Propanone + Aniline, + N-Methylaniline, or + Pyridine Systems
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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