Glycerin
- Formula: C3H8O3
- Molecular weight: 92.0938
- IUPAC Standard InChIKey: PEDCQBHIVMGVHV-UHFFFAOYSA-N
- CAS Registry Number: 56-81-5
- 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. - Other names: 1,2,3-Propanetriol; Glycerol; Glycerine; Glyceritol; Glycyl alcohol; Glyrol; Glysanin; Osmoglyn; Propanetriol; Trihydroxypropane; Synthetic glycerin; 90 Technical glycerin; Dagralax; Glycerin, anhydrous; Glycerin, synthetic; Ophthalgan; Synthetic glycerine; Vitrosupos; 1,2,3-Trihydroxypropane; 90 Technical glycerine; Clyzerin, wasserfrei; Grocolene; MOON; Star; Optim; Bulbold; Cristal; Emery 912; Incorporation factor; Pricerine 9091; Propane-1,2,3-triol; Emery 916; IFP; NSC 9230; Auralgan (Salt/Mix); Collyrium Fresh-Eye Drops (Salt/Mix)
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, 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
DRB - Donald R. Burgess, Jr.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -577.9 ± 1.1 | kJ/mol | Ccb | Bastos, Nilsson, et al., 1988 | Uc=-1653.1±0.4 kJ/mol; ALS |
ΔfH°gas | -576.9 | kJ/mol | N/A | Parks, West, et al., 1946 | Value computed using ΔfHliquid° value of -668.6±0.4 kj/mol from Parks, West, et al., 1946 and ΔvapH° value of 91.7 kj/mol from Bastos, Nilsson, et al., 1988.; DRB |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, 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 | -669.6 ± 0.6 | kJ/mol | Ccb | Bastos, Nilsson, et al., 1988 | Uc=-1653.1±0.4 kJ/mol; ALS |
ΔfH°liquid | -668.60 ± 0.42 | kJ/mol | Ccb | Parks, West, et al., 1946 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1654.3 ± 0.4 | kJ/mol | Ccb | Bastos, Nilsson, et al., 1988 | Uc=-1653.1±0.4 kJ/mol; Corresponding ΔfHºliquid = -669.6 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1654.1 | kJ/mol | Cm | Parks and Manchester, 1952 | From heat of solution; Corresponding ΔfHºliquid = -669.73 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1655.3 ± 1.0 | kJ/mol | Ccb | Parks, West, et al., 1946 | Corresponding ΔfHºliquid = -668.52 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1665.1 | kJ/mol | Ccb | Emery and Benedict, 1911 | Corresponding ΔfHºliquid = -658.8 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 37.87 | J/mol*K | N/A | Ahlberg, Blanchard, et al., 1937 | DH |
S°solid,1 bar | 42.34 | J/mol*K | N/A | Ahlberg, Blanchard, et al., 1937 | glass phase; Value S-S0; zero point entropy calculated as 19.41 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
218.9 | 298.15 | Bastos, Nilsson, et al., 1988 | DH |
229.3 | 313.15 | Chen and Ge, 1982 | T = 20 to 60 K. Cp given as 2.49 kJ/kg*K at 40°C. Cp at 25°C estimated from graph to be ca. 2.43 kJ/kg*K or 223 J/mol*K.; DH |
219.2 | 293.15 | Atalla, El-Sharkawy, et al., 1981 | DH |
221.9 | 298.15 | Murthy and Subrahmanyam, 1977 | DH |
221.7 | 301.2 | Paz Andrade, Paz, et al., 1970 | T = 28, 40°C.; DH |
221.18 | 293.15 | Omel'chenko, 1962 | T = 273 to 523 K. A reexamination of the literature. Cp(liq) = 32.9 + 0.0761T - 0.0000269T2(T in K) cal/mol*K (0 to 250°C).; DH |
218.5 | 298. | Rabinovich and Nikolaev, 1962 | T = 10 to 55°C.; DH |
213.8 | 298. | Ernst, Watkins, et al., 1936 | DH |
207.9 | 298.1 | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 41.4 J/mol*K.; DH |
223.4 | 299.4 | Gibson and Giauque, 1923 | T = 70.2 to 299.4 K. Value is unsmoothed experimental datum. Cp also measured for glass.; DH |
225.9 | 289.7 | Simon, 1922 | T = 19 to 294 K. Value is unsmoothed experimental datum. Cp also measured for glass.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
49.79 | 86.92 | Ahlberg, Blanchard, et al., 1937 | T = 3 to 87 K. Value is unsmoothed experimental datum.; DH |
50.21 | 85.12 | Ahlberg, Blanchard, et al., 1937 | glass phase; T = 2.3 to 95 K. Value is unsmoothed experimental datum.; DH |
150. | 279. to 284. | Volmer and Marder, 1931 | T = 279 to 284 K. Cp measured for the solid phase is an average value over the temperature range.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 550. ± 40. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 290. ± 5. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 291.8 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.2 K; TRC |
Ttriple | 291.0 | K | N/A | Gibson and Giauque, 1923 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 850. | K | N/A | Nikitin, Pavlov, et al., 1993 | Uncertainty assigned by TRC = 4. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 75.00 | bar | N/A | Nikitin, Pavlov, et al., 1993 | Uncertainty assigned by TRC = 2.00 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 91.7 ± 0.9 | kJ/mol | C | Bastos, Nilsson, et al., 1988 | Uc=-1653.1±0.4 kJ/mol; ALS |
ΔvapH° | 91.7 | kJ/mol | N/A | Bastos, Nilsson, et al., 1988 | DRB |
ΔvapH° | 91.7 ± 0.9 | kJ/mol | C | Bastos, Nilsson, et al., 1988 | AC |
ΔvapH° | 85.8 | kJ/mol | V | Ross and Heideger, 1962 | ALS |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
455.2 | 0.027 | Aldrich Chemical Company Inc., 1990 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
78.5 | 484. | A | Stephenson and Malanowski, 1987 | Based on data from 469. to 563. K.; AC |
85.8 | 308. | ME | Stephenson and Malanowski, 1987 | Based on data from 293. to 343. K. See also Ross and Heideger, 1962 and Dykyj, 1970.; AC |
86.8 | 316. | ME | Cammenga, Schulze, et al., 1977 | Based on data from 291. to 341. K.; AC |
67.5 | 343. | GC | Nováková and Novák, 1977 | AC |
66.8 | 353. | GC | Nováková and Novák, 1977 | AC |
66.2 | 363. | GC | Nováková and Novák, 1977 | AC |
65.5 | 373. | GC | Nováková and Novák, 1977 | AC |
64.8 | 383. | GC | Nováková and Novák, 1977 | AC |
71.5 | 300. | N/A | McFeely and Somorjai, 1972 | Based on data from 278. to 323. K.; AC |
86. | 471. | N/A | Richardson, 1886 | Based on data from 456. to 553. K.; AC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
456.40 to 533.6 | 3.93737 | 1411.531 | -200.566 | Richardson, 1886, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
18.303 | 292. | Yoshida, 1944 | DH |
18.285 | 291.0 | Gibson and Giauque, 1923 | DH |
18.28 | 293. | Acree, 1991 | AC |
18.476 | 291.75 | Volmer and Marder, 1931 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
62.7 | 292. | Yoshida, 1944 | DH |
62.8 | 291.0 | Gibson and Giauque, 1923 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, 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 |
---|---|---|---|---|
>6.0×10+8 | E | N/A | Value obtained by missing citation using the group contribution method. | |
<4.0×10+11 | E | N/A | Value obtained by missing citation using the group contribution method. | |
60000. | M | N/A | missing citation say that this value is unreliable. |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, 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
Data compiled as indicated in comments:
MM - Michael M. Meot-Ner (Mautner)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Proton affinity (review) | 874.8 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 820. | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
>840.7 | Bouchoux, Buisson, et al., 2003 | MM |
>835.8 | Bouchoux, Buisson, et al., 2003 | MM |
>848.6 ± 1.2 | Bouchoux, Buisson, et al., 2003 | MM |
Gas basicity at 298K
Gas basicity (review) (kJ/mol) | Reference | Comment |
---|---|---|
810.2 | Bouchoux, Buisson, et al., 2003 | MM |
805.5 | Bouchoux, Buisson, et al., 2003 | MM |
818.9 ± 0.5 | Bouchoux, Buisson, et al., 2003 | MM |
References
Go To: Top, Gas phase thermochemistry data, 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.
Bastos, Nilsson, et al., 1988
Bastos, M.; Nilsson, S-O.; Ribeiro Da Silva, M.D.M.C.; Ribeiro Da Silva, M.A.V.; Wadso, I.,
Thermodynamic properties of glycerol enthalpies of combustion and vaporization and the heat capacity at 298.15 K. Enthalpies of solution in water at 288.15, 298.15, and 308.15 K,
J. Chem. Thermodyn., 1988, 20, 1353-1359. [all data]
Parks, West, et al., 1946
Parks, G.S.; West, T.J.; Naylor, B.F.; Fujii, P.S.; McClaine, L.A.,
Thermal data on organic compounds. XXIII. Modern combustion data for fourteen hydrocarbons and five polyhydroxy alcohols,
J. Am. Chem. Soc., 1946, 68, 2524-2527. [all data]
Parks and Manchester, 1952
Parks, G.S.; Manchester, K.E.,
The heats of solution of erythritol, mannitol and dulcitol; combustion values for liquid polyhydroxy alcohols,
J. Am. Chem. Soc., 1952, 74, 3435-34. [all data]
Emery and Benedict, 1911
Emery, A.G.; Benedict, F.G.,
The heat of combustion of compounds of physiological importance,
Am. J. Physiol., 1911, 28, 301-307. [all data]
Ahlberg, Blanchard, et al., 1937
Ahlberg, J.E.; Blanchard, E.R.; Lundberg, W.O.,
The heat capacities of benzene, methyl alcohol and glycerol at very low temperatures,
J. Chem. Phys., 1937, 5, 537-551. [all data]
Chen and Ge, 1982
Chen, Z.S.; Ge, X.S.,
A multifunctional apparatus for the simultaneous measurement of the specific heat, thermal conductivity and heat of fusion of materials undergoing phase transformations, Proc. Symp. Thermophys. Prop.,
8th, 1982, (2), 115-121. [all data]
Atalla, El-Sharkawy, et al., 1981
Atalla, S.R.; El-Sharkawy, A.A.; Gasser, F.A.,
Measurement of thermal properties of liquids with an AC heated-wire technique,
Inter. J. Thermophys., 1981, 2(2), 155-162. [all data]
Murthy and Subrahmanyam, 1977
Murthy, N.M.; Subrahmanyam, S.V.,
Behaviour of excess heat capacity of aqueous non-electrolytes,
Indian J. Pure Appl. Phys., 1977, 15, 485-489. [all data]
Paz Andrade, Paz, et al., 1970
Paz Andrade, M.I.; Paz, J.M.; Recacho, E.,
Contribucion a la microcalorimetria de los calores especificos de solidos y liquidos,
An. Quim., 1970, 66, 961-967. [all data]
Omel'chenko, 1962
Omel'chenko, F.S.,
On the heat capacity of glycerol, Izv. Vysshikh. Uchebn. Zaved.,
Pishchevaya Tekhnol., 1962, (3), 97-98. [all data]
Rabinovich and Nikolaev, 1962
Rabinovich, I.B.; Nikolaev, P.N.,
Isotopic effect in the specific heat of some deutero compounds,
Dokl. Akad. Nauk, 1962, SSSR 142, 1335-1338. [all data]
Ernst, Watkins, et al., 1936
Ernst, R.C.; Watkins, C.H.; Ruwe, H.H.,
The physical properties of the ternary system ethyl alcohol-glycerin-water,
J. Phys. Chem., 1936, 40, 627-635. [all data]
Parks, Kelley, et al., 1929
Parks, G.S.; Kelley, K.K.; Huffman, H.M.,
Thermal data on organic compounds. V. A revision of the entropies and free energies of nineteen organic compounds,
J. Am. Chem. Soc., 1929, 51, 1969-1973. [all data]
Gibson and Giauque, 1923
Gibson, G.E.; Giauque, W.F.,
The third law of thermodynamics. Evidence from the specific heats of glycerol that the entropy of a glass exceeds that of a crystal at the absolute zero,
J. Am. Chem. Soc., 1923, 45, 93-104. [all data]
Simon, 1922
Simon, F.,
Untersuchungen über die spezifische Wärme bei tiefen Temperaturen,
Ann. Physik. [4], 1922, 68, 241-280. [all data]
Volmer and Marder, 1931
Volmer, M.; Marder, M.,
Zur theorie der linearen kristallistionsgeschwindigkeit unterkuhlter schmelzen und unterkuhlter fester modifikationen,
Z. Physik. Chem., 1931, 154A, 97-112. [all data]
Wilhoit, Chao, et al., 1985
Wilhoit, R.C.; Chao, J.; Hall, K.R.,
Thermodynamic Properties of Key Organic Compounds in the Carbon Range C1 to C4. Part 1. Properties of Condensed Phases,
J. Phys. Chem. Ref. Data, 1985, 14, 1. [all data]
Nikitin, Pavlov, et al., 1993
Nikitin, E.D.; Pavlov, P.A.; Skripov, P.V.,
Measurement of the critical properties of thermally unstable substances and mixtures by the pulse-heating method,
J. Chem. Thermodyn., 1993, 25, 869-80. [all data]
Ross and Heideger, 1962
Ross, G.R.; Heideger, W.J.,
Vapor pressure of glycerol,
J. Chem. Eng. Data, 1962, 7, 505-507. [all data]
Aldrich Chemical Company Inc., 1990
Aldrich Chemical Company Inc.,
Catalog Handbook of Fine Chemicals, Aldrich Chemical Company, Inc., Milwaukee WI, 1990, 1. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2
. [all data]
Dykyj, 1970
Dykyj, J.,
Petrochemica, 1970, 10, 2, 51. [all data]
Cammenga, Schulze, et al., 1977
Cammenga, Heiko K.; Schulze, Friedrich W.; Theuerl, Wilhelm,
Vapor pressure and evaporation coefficient of glycerol,
J. Chem. Eng. Data, 1977, 22, 2, 131-134, https://doi.org/10.1021/je60073a004
. [all data]
Nováková and Novák, 1977
Nováková, N.; Novák, J.,
Measurement of heats of vaporization by means of a gas chromatograph,
Journal of Chromatography A, 1977, 135, 1, 13-24, https://doi.org/10.1016/S0021-9673(00)86297-4
. [all data]
McFeely and Somorjai, 1972
McFeely, F.R.; Somorjai, G.A.,
Vaporization kinetics of hydrogen-bonded liquids,
J. Phys. Chem., 1972, 76, 6, 914-918, https://doi.org/10.1021/j100650a022
. [all data]
Richardson, 1886
Richardson, Arthur,
LXXIII.?Determinations of vapour-pressures of alcohols and organic acids, and the relations existing between the vapour-pressures of the alcohols and organic acids,
J. Chem. Soc., Trans., 1886, 49, 761, https://doi.org/10.1039/ct8864900761
. [all data]
Richardson, 1886, 2
Richardson, A.,
LXXIII. Determinations of Vapour-Pressures of Alcohols and Organic Acids, and the Relations Existing Between the Vapour-Pressures of the Alcohols and Organic Acids,
J. Chem. Soc., 1886, 49, 761-776, https://doi.org/10.1039/ct8864900761
. [all data]
Yoshida, 1944
Yoshida, U.,
Structural relaxation of amorphous solids and the cybotactic structure of super-cooled liquids,
Mem. Coll. Sci. Kyoto Imp. Univ., 1944, 24A, 135-148. [all data]
Acree, 1991
Acree, William E.,
Thermodynamic properties of organic compounds: enthalpy of fusion and melting point temperature compilation,
Thermochimica Acta, 1991, 189, 1, 37-56, https://doi.org/10.1016/0040-6031(91)87098-H
. [all data]
Hunter and Lias, 1998
Hunter, E.P.; Lias, S.G.,
Evaluated Gas Phase Basicities and Proton Affinities of Molecules: An Update,
J. Phys. Chem. Ref. Data, 1998, 27, 3, 413-656, https://doi.org/10.1063/1.556018
. [all data]
Bouchoux, Buisson, et al., 2003
Bouchoux, G.; Buisson, D.A.; Bourcier, S.; Sablier, M.,
Application of the kinetic method to bifunctional bases. ESI tandem quadrupole experiments,
Int. J. Mass Spectrom., 2003, 228, 1035. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid Pc Critical pressure S°solid,1 bar Entropy of solid at standard conditions (1 bar) Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion 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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