Pyridine
- Formula: C5H5N
- Molecular weight: 79.0999
- IUPAC Standard InChIKey: JUJWROOIHBZHMG-UHFFFAOYSA-N
- CAS Registry Number: 110-86-1
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Isotopologues:
- Other names: Azabenzene; Azine; NCI-C55301; Piridina; Pirydyna; Pyridin; Rcra waste number U196; UN 1282; Pyr; CP 32; NSC 406123
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
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Condensed phase thermochemistry data
Go To: Top, Phase change data, Henry's Law data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | 99.96 ± 0.50 | kJ/mol | Ccb | Hubbard, Frow, et al., 1961 | ALS |
ΔfH°liquid | 100.2 ± 1.5 | kJ/mol | Ccb | Cox, Challoner, et al., 1954 | ALS |
ΔfH°liquid | 69.9 | kJ/mol | Ccb | Constam and White, 1903 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2725. | kJ/mol | Ccb | Strepikheev, Baranov, et al., 1962 | ALS |
ΔcH°liquid | -2782.2 ± 0.42 | kJ/mol | Ccb | Hubbard, Frow, et al., 1961 | ALS |
ΔcH°liquid | -2782.4 ± 1.5 | kJ/mol | Ccb | Cox, Challoner, et al., 1954 | ALS |
ΔcH°liquid | -2758. | kJ/mol | Ccb | Constam and White, 1903 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 177.90 | J/mol*K | N/A | McCullough, Douslin, et al., 1957 | DH |
S°liquid | 179.1 | J/mol*K | N/A | Parks, Todd, et al., 1936 | Extrapolation below 90 K, 50.04 J/mol*K.; DH |
S°liquid | 210.41 | J/mol*K | N/A | Pearce and Bakke, 1936 | Extrapolation below 90 K, 89.33 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
193.4 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 353 K.; DH |
133. | 298.15 | Hubbard, Frow, et al., 1961 | DH |
146.9 | 332. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 22 to 96°C.; DH |
132.72 | 298.15 | McCullough, Douslin, et al., 1957 | T = 10 to 350 K.; DH |
134.93 | 298.1 | Parks, Todd, et al., 1936 | T = 90 to 300 K.; DH |
133.30 | 298.1 | Pearce and Bakke, 1936 | T = 90 to 298 K. Value is unsmoothed experimental datum.; DH |
129.3 | 289. | Radulescu and Jula, 1934 | DH |
135.35 | 273.4 | Swietoslawski, Tybicka, et al., 1931 | DH |
135.6 | 290. | Swietoslawski, Tybicka, et al., 1931, 2 | DH |
129.33 | 294. | Mathews, Krause, et al., 1917 | DH |
130.5 | 283. | Bramley, 1916 | Mean value, 0 to 20°C.; DH |
Phase change data
Go To: Top, Condensed phase thermochemistry data, Henry's Law data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 388.5 ± 0.6 | K | AVG | N/A | Average of 80 out of 84 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 232. ± 2. | K | AVG | N/A | Average of 26 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 231.48 | K | N/A | Helm, Lanum, et al., 1958 | Uncertainty assigned by TRC = 0.03 K; measured in calorimeter at USBM, Bartlesville, OK; TRC |
Ttriple | 231.480 | K | N/A | McCullough, Douslin, et al., 1957, 2 | Uncertainty assigned by TRC = 0.05 K; by extrapolation of 1/f to zero; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 619. ± 2. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 56.60 | bar | N/A | Brunner, 1987 | Uncertainty assigned by TRC = 0.0565 bar; Visual, optical cell 30cm high. P transducer cal. vs PB.; TRC |
Pc | 56.40 | bar | N/A | Kobe, Ravicz, et al., 1956 | Uncertainty assigned by TRC = 1.034 bar; TRC |
Pc | 60.795 | bar | N/A | Herz and Neukirch, 1923 | Uncertainty assigned by TRC = 0.8106 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.253 | l/mol | N/A | Kobe, Ravicz, et al., 1956 | Uncertainty assigned by TRC = 0.005 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 40.3 ± 0.3 | kJ/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
35.09 | 388.4 | N/A | Majer and Svoboda, 1985 | |
39.3 | 324. | N/A | Ukraintseva, Soldatov, et al., 1997 | Based on data from 289. to 358. K.; AC |
37.6 | 354. | N/A | Blanco, Beltran, et al., 1994 | Based on data from 346. to 362. K.; AC |
39.9 | 310. | EB | Lencka, 1990 | Based on data from 295. to 388. K.; AC |
39.7 | 311. | A | Stephenson and Malanowski, 1987 | Based on data from 296. to 353. K.; AC |
37.3 | 363. | A | Stephenson and Malanowski, 1987 | Based on data from 348. to 434. K.; AC |
35.0 | 446. | A | Stephenson and Malanowski, 1987 | Based on data from 431. to 558. K.; AC |
34.0 | 567. | A | Stephenson and Malanowski, 1987 | Based on data from 552. to 620. K.; AC |
37.6 | 355. | EB | Stephenson and Malanowski, 1987 | Based on data from 340. to 426. K. See also McCullough, Douslin, et al., 1957.; AC |
39.6 | 313. | C | Michou-Saucet, Jose, et al., 1986 | Based on data from 298. to 333. K.; AC |
39.4 | 313. | C | Majer, Svoboda, et al., 1984 | AC |
38.5 | 328. | C | Majer, Svoboda, et al., 1984 | AC |
37.7 | 343. | C | Majer, Svoboda, et al., 1984 | AC |
36.3 | 368. | N/A | Majer, Svoboda, et al., 1984 | AC |
37.5 ± 0.1 | 346. | C | McCullough, Douslin, et al., 1957 | AC |
36.4 ± 0.1 | 366. | C | McCullough, Douslin, et al., 1957 | AC |
35.1 ± 0.1 | 388. | C | McCullough, Douslin, et al., 1957 | AC |
38.4 | 335. | MG | Herington and Martin, 1953 | Based on data from 320. to 388. K.; AC |
44.4 | 273. | N/A | Meulen and Mann, 1931 | Based on data from 258. to 389. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 388. | 55.43 | 0.2536 | 620. | Majer and Svoboda, 1985 |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
340.5 to 426.04 | 4.16272 | 1371.358 | -58.496 | McCullough, Douslin, et al., 1957 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.2785 | 231.49 | McCullough, Douslin, et al., 1957 | Includes energy of anomaly at about 210 K.; DH |
8.28 | 231.5 | Domalski and Hearing, 1996 | AC |
8.272 | 231.1 | Parks, Todd, et al., 1936 | DH |
3.100 | 230.38 | Pearce and Bakke, 1936 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.76 | 231.49 | McCullough, Douslin, et al., 1957 | Includes; DH |
35.79 | 231.1 | Parks, Todd, et al., 1936 | DH |
13.46 | 230.38 | Pearce and Bakke, 1936 | DH |
Henry's Law data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
89. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
110. | 5900. | M | N/A |
Gas phase ion energetics data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.26 ± 0.01 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 930. | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 898.1 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
936.5 ± 8.5 | Wind, Papp, et al., 2005 | T = 298K; MM |
Protonation entropy at 298K
Protonation entropy (J/mol*K) | Reference | Comment |
---|---|---|
-1. ± 10. | Wind, Papp, et al., 2005 | T = 298K; MM |
Ionization energy determinations
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C3H3+ | 14.00 ± 0.10 | ? | EI | Momigny, Urbain, et al., 1965 | RDSH |
C3H3N+ | 13.84 ± 0.10 | C2H2 | EI | Momigny, Urbain, et al., 1965 | RDSH |
C4H2+ | 16.17 ± 0.10 | HCN+H2 | EI | Momigny, Urbain, et al., 1965 | RDSH |
C4H3+ | 16.61 ± 0.10 | HCN+H | EI | Momigny, Urbain, et al., 1965 | RDSH |
C4H4+ | 11.84 ± 0.05 | HCN | TRPI | Lifshitz and Malinovich, 1984 | LBLHLM |
C4H4+ | 12.6 ± 0.1 | HCN | EI | Burgers and Holmes, 1984 | LBLHLM |
C4H4+ | 12.34 ± 0.05 | HCN | EI | Burgers and Holmes, 1984 | LBLHLM |
C4H4+ | 12.0 ± 0.2 | HCN | TRPI | Lifshitz, 1982 | LBLHLM |
C4H4+ | 12.15 ± 0.02 | HCN | PIPECO | Rosenstock, Stockbauer, et al., 1981 | LLK |
C4H4+ | 11.8 | HCN | PI | Eland, Berkowitz, et al., 1978 | LLK |
C4H4+ | 12.3 ± 0.1 | HCN | EI | Rosenstock, McCulloh, et al., 1977 | LLK |
C4H4+ | 13.41 ± 0.05 | HCN | EI | Zaretskii, Oren, et al., 1976 | LLK |
C4H4+ | 13.28 | HCN | EI | Beynon, Hopkinson, et al., 1969 | RDSH |
C5H3N+ | 12.42 ± 0.10 | H2 | EI | Momigny, Urbain, et al., 1965 | RDSH |
C5H4N+ | 14.00 ± 0.10 | H | EI | Momigny, Urbain, et al., 1965 | RDSH |
De-protonation reactions
C5H4N- + =
By formula: C5H4N- + H+ = C5H5N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1631. ± 8.4 | kJ/mol | IMRE | Schafman and Wenthold, 2007 | gas phase; B |
ΔrH° | 1636. ± 10. | kJ/mol | TDEq | Meot-ner and Kafafi, 1988 | gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1601. ± 8.4 | kJ/mol | TDEq | Meot-ner and Kafafi, 1988 | gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B |
ΔrG° | 1607. ± 13. | kJ/mol | IMRB | DePuy, Kass, et al., 1988 | gas phase; Comparable to water in acidity; B |
ΔrG° | <1574. ± 8.4 | kJ/mol | IMRB | Bruins, Ferrer-Correia, et al., 1978 | gas phase; O- deprotonates; B |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Hubbard, Frow, et al., 1961
Hubbard, W.N.; Frow, F.R.; Waddington, G.,
The heats of combustion and formation of pyridine and hippuric acid,
J. Phys. Chem., 1961, 65, 1326-1328. [all data]
Cox, Challoner, et al., 1954
Cox, J.D.; Challoner, A.R.; Meetham, A.R.,
The heats of combustion of pyridine and certain of its derivatives,
J. Chem. Soc., 1954, 265-271. [all data]
Constam and White, 1903
Constam, E.J.; White, J.,
Physico-chemical investigations in the pyridine series,
Am. Chem. J., 1903, 29, 1-49. [all data]
Strepikheev, Baranov, et al., 1962
Strepikheev, Yu.A.; Baranov, Yu.I.; Burmistrova, O.A.,
Determination of the heats of combustion and the heat capacities of several mono- and di-isocyanates,
Izv. Vyssh. Uchebn. Zaved., Khim. Khim. Tekhnol., 1962, 5, 387-390. [all data]
McCullough, Douslin, et al., 1957
McCullough, J.P.; Douslin, D.R.; Messerly, J.F.; Hossenlopp, I.A.; Kincheloe, T.C.; Waddington, G.,
Pyridine: experimental and calculated chemical thermodynamic properties between 0 and 1500 K., a revised vibrational assignment,
J. Am. Chem. Soc., 1957, 79, 4289-4295. [all data]
Parks, Todd, et al., 1936
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Pearce and Bakke, 1936
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The heat capacity and the free energy of formation of pyridine,
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Rastorguev and Ganiev, 1967
Rastorguev, Yu.L.; Ganiev, Yu.A.,
Study of the heat capacity of selected solvents,
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Swietoslawski and Zielenkiewicz, 1958
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Mean specific heat of some ternary azeotropes,
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Radulescu and Jula, 1934
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Beiträge zur Bestimmung der Abstufung der Polarität des Aminstickstoffes in den organischen Verbindungen,
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Sur un microcalorimetre adiabatique, adapte aux mesures de la chaleur specifique de substances solides et liquides,
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Swietoslawski, Tybicka, et al., 1931, 2
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Sur un microcalorimetre adiabatique, adapte aux mesures de la chaleur specifique de substances solides et liquides,
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Mathews, Krause, et al., 1917
Mathews, J.H.; Krause, E.L.; Bohnson, B.L.,
a contribution to the thermal chemistry of pyridine,
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Bramley, 1916
Bramley, A.,
The study of binary mixtures. Part IV. Heats of reaction and specific heats,
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Purification and Properties of Pyrrole, Pyrrolidine, Pyridine and 2-Methylpyridine,
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Pyridine: Experimental and Calculated Chemical Thermodynamic Prop- erties Between 0 and 1500 K; A Revised Vibrational Assignment,
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Kobe, K.A.; Ravicz, A.E.; Vohra, S.P.,
Critical Properties and Vapor Pressures of Some Ethers and Heterocyclic Compounds,
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Herz and Neukirch, 1923
Herz, W.; Neukirch, E.,
On Knowldge of the Critical State,
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Ukraintseva, E.A.; Soldatov, D.V.; Dyadin, Yu.A.,
Pyridine vapor pressure and thermodynamic parameters of clathrate and complex formation in the pyridine-zinc nitrate system,
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Blanco, Beatriz; Beltran, Sagrario; Cabezas, Jose Luis; Coca, Jose,
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Measurements of the vapour pressures of pyridine, 2-methylpyridine, 2,4-dimethylpyridine, 2,6-dimethylpyridine, and 2,4,6-trimethylpyridine from 0.1 kPa to atmospheric pressure using a modified Swietoslawski ebulliometer,
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Proton Affinity of beta-Oxalylaminoalanine (BOAA): Incorporation of Direct Entropy Correction into the Single-Reference Kinetic Method,
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Threshold electron-impact excitation spectrum of pyridine,
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The ionisation potential of some substituted pyridines,
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Akopyan and Vilesov, 1964
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Excited states of positive ions and dissociative photoionization of aromatic amines,
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Charge transfer in organic solids, induced by light,
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Ionization potentials of some molecules,
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Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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