1-Decanol
- Formula: C10H22O
- Molecular weight: 158.2811
- IUPAC Standard InChIKey: MWKFXSUHUHTGQN-UHFFFAOYSA-N
- CAS Registry Number: 112-30-1
- 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. - Species with the same structure:
- Other names: Decyl alcohol; n-Decan-1-ol; n-Decanol; n-Decyl alcohol; Alcohol C10; Alfol 10; Capric alcohol; Caprinic alcohol; Decanol; Nonylcarbinol; Sipol L10; T-148; Decylic Alcohol; Decan-1-ol; Decanol-(1); Agent 504; Antak; Dytol S-91; Decyl, n- alcohol; Lorol 22; Primary decyl alcohol; Royaltac; C 10 alcohol; Epal 10; Royaltac-85; Royaltac M-2; Lorol C10; Nonylcacarbinol; 1-Hydroxydecane; Conol 10N; Kalcohl 10H; NSC 406313; Nacol 10-99
- Information on this page:
- Other data available:
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Gas phase thermochemistry data
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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:
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -395. ± 10. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Condensed phase thermochemistry data
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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.
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -478.1 ± 1.1 | kJ/mol | Ccb | Mosselman and Dekker, 1975 | ALS |
ΔfH°liquid | -479.74 ± 0.96 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; ALS |
ΔfH°liquid | -486.1 ± 3.3 | kJ/mol | Ccb | Green, 1960 | ALS |
ΔfH°liquid | -486.1 ± 3.0 | kJ/mol | Ccb | Verkade and Coops, 1927 | estimated uncertainty; DRB |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -6619. ± 8. | kJ/mol | Ccb | Freeman and Bagby, 1989 | Corresponding ΔfHºliquid = -460. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -6601.1 ± 1.1 | kJ/mol | Ccb | Mosselman and Dekker, 1975 | Corresponding ΔfHºliquid = -478.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -6599.63 ± 0.75 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; Corresponding ΔfHºliquid = -479.61 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -6593.3 ± 3.3 | kJ/mol | Ccb | Green, 1960 | Corresponding ΔfHºliquid = -485.97 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -6593.1 | kJ/mol | Ccb | Verkade and Coops, 1927 | Corrected for 298 and 1 atm.; Corresponding ΔfHºliquid = -486.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
372.98 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
387.8 | 304.05 | Naziev and Bashirov, 1988 | T = 304 to 497 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.45 kJ/kg*K. Cp data given at pressures from 0.1 to 50 MPa.; DH |
369.96 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
377.8 | 305.79 | Griigo'ev, Yanin, et al., 1979 | T = 305 to 463 K. p = 0.98 bar.; DH |
377. | 301. | Svensson, 1979 | T = 301 to 461 K.; DH |
377.30 | 303.15 | Woycicka and Kalinowska, 1975 | DH |
Phase change data
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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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
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 | 505. ± 3. | K | AVG | N/A | Average of 16 out of 17 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 279.6 | K | N/A | Davies and Kybett, 1965 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 280.05 | K | N/A | Costello and Bowden, 1958 | Uncertainty assigned by TRC = 0.4 K; TRC |
Tfus | 277. | K | N/A | Badin, 1943 | Uncertainty assigned by TRC = 3. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 279.65 | K | N/A | Spizzichino, 1956 | Uncertainty assigned by TRC = 1. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.000001 | bar | N/A | Spizzichino, 1956 | Uncertainty assigned by TRC = 1.3×10-7 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 690. ± 10. | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 23.2 ± 0.5 | bar | N/A | Gude and Teja, 1995 | |
Pc | 23.10 | bar | N/A | Quadri, Khilar, et al., 1991 | Uncertainty assigned by TRC = 0.60 bar; TRC |
Pc | 23.20 | bar | N/A | Rosenthal and Teja, 1990 | Uncertainty assigned by TRC = 0.20 bar; TRC |
Pc | 23.20 | bar | N/A | Rosenthal and Teja, 1989 | Uncertainty assigned by TRC = 0.20 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.649 | l/mol | N/A | Gude and Teja, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 1.54 ± 0.05 | mol/l | N/A | Gude and Teja, 1995 | |
ρc | 1.67 | mol/l | N/A | Teja, Lee, et al., 1989 | TRC |
ρc | 1.54 | mol/l | N/A | Anselme and Teja, 1988 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 1.67 | mol/l | N/A | Efremov, 1966 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 82. ± 6. | kJ/mol | AVG | N/A | Average of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 112.5 ± 6.3 | kJ/mol | N/A | Karnes, Kybett, et al., 1965 | AC |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
380.7 | 0.009 | Weast and Grasselli, 1989 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
78.180 | 323.15 | N/A | Svensson, 1979 | No pressure measurement.; DH |
79.5 | 309. | GS | Kulikov, Verevkin, et al., 2001 | Based on data from 281. to 327. K.; AC |
81.1 | 293. | N/A | N'Guimbi, Berro, et al., 1999 | Based on data from 278. to 378. K.; AC |
75.4 | 336. | N/A | N'Guimbi, Kasehgari, et al., 1992 | Based on data from 283. to 388. K.; AC |
71.6 | 364. | A | Stephenson and Malanowski, 1987 | Based on data from 349. to 410. K.; AC |
62.6 | 420. | A | Stephenson and Malanowski, 1987 | Based on data from 405. to 528. K.; AC |
53.9 | 489. | A | Stephenson and Malanowski, 1987 | Based on data from 474. to 529. K.; AC |
78.2 ± 0.8 | 323. | C | Svensson, 1979 | AC |
77.6 | 313. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 298. to 325. K.; AC |
69.5 | 393. | DTA | Kemme and Kreps, 1969 | Based on data from 378. to 504. K.; AC |
77.6 | 311. | ME | Davies and Kybett, 1965 | Based on data from 298. to 325. K.; AC |
69.6 | 379. | N/A | Rose, Papahronis, et al., 1958 | Based on data from 364. to 461. 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 323. | 122.27 | 0.4044 | 687. | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
241.93 | 323.15 | Svensson, 1979 | No; DH |
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 |
---|---|---|---|---|---|
349.37 to 406.18 | 4.53321 | 1742.392 | -115.236 | Ambrose, Ellender, et al., 1974 | Coefficents calculated by NIST from author's data. |
400.41 to 528.32 | 3.85752 | 1373.019 | -147.727 | Ambrose and Sprake, 1970 | Coefficents calculated by NIST from author's data. |
378. to 504. | 3.51869 | 1180.306 | -168.829 | Kemme and Kreps, 1969 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
115.5 ± 6.3 | 268. | ME | Karnes, Kybett, et al., 1965 | Based on data from 264. to 273. K. See also Stephenson and Malanowski, 1987.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.67 | 280. | van Miltenburg, Gabrielová, et al., 2003 | AC |
37.66 | 280.1 | Domanska and Gonzalez, 1997 | AC |
Henry's Law data
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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 |
---|---|---|---|---|
37. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. |
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 compiled by: John E. Bartmess
De-protonation reactions
C10H21O- + =
By formula: C10H21O- + H+ = C10H22O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1560. ± 8.4 | kJ/mol | CIDC | Haas and Harrison, 1993 | gas phase; CIDC at 50 eV 1.0 kcal/mol weaker than metastable value. |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1533. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; CIDC at 50 eV 1.0 kcal/mol weaker than metastable value. |
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.
Mosselman and Dekker, 1975
Mosselman, C.; Dekker, H.,
Enthalpies of formation of n-alkan-1-ols,
J. Chem. Soc. Faraday Trans. 1, 1975, 417-424. [all data]
Chao and Rossini, 1965
Chao, J.; Rossini, F.D.,
Heats of combustion, formation, and isomerization of nineteen alkanols,
J. Chem. Eng. Data, 1965, 10, 374-379. [all data]
Rossini, 1934
Rossini, F.D.,
Heats of combustion and of formation of the normal aliphatic alcohols in the gaseous and liquid states, and the energies of their atomic linkages,
J. Res. NBS, 1934, 13, 189-197. [all data]
Green, 1960
Green, J.H.S.,
Revision of the values of the heats of formation of normal alcohols,
Chem. Ind. (London), 1960, 1215-1216. [all data]
Verkade and Coops, 1927
Verkade, P.E.; Coops, J., Jr.,
Calorimetric researches XIV. Heats of combustion of successive members of homologous series: the normal primary aliphatic alcohols,
Recl. Trav. Chim. Pays-Bas, 1927, 46, 903-917. [all data]
Freeman and Bagby, 1989
Freeman, B.; Bagby, M.O.,
Heats of combustion of fatty esters and triglycerides,
J. Am. Oil Chem. Soc., 1989, 66, 1601-1605. [all data]
Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M.,
Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc.,
Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]
Naziev and Bashirov, 1988
Naziev, Ya.M.; Bashirov, M.M.,
Isobaric specific heats of higher alcohols at elevated pressures,
Teplofiz. Vysok. Temp., 1988, 26, 58-62. [all data]
Costas and Patterson, 1985
Costas, M.; Patterson, D.,
Self-association of alcohols in inert solvents, J. Chem. Soc.,
Faraday Trans. 1, 1985, 81, 635-654. [all data]
Griigo'ev, Yanin, et al., 1979
Griigo'ev, B.A.; Yanin, G.S.; Rastorguev, Yu.L.; Thermophysical parameters of alcohols, Tr. GIAP,
54, 1979, 57-64. [all data]
Svensson, 1979
Svensson, Ch.,
Enthalpies of vaporization of 1-decanol and 1-dodecanol and their influence on the CH2-increment for the enthalpies of formation,
J. Chem. Thermodynam., 1979, 11, 593-596. [all data]
Woycicka and Kalinowska, 1975
Woycicka, M.K.; Kalinowska, B.,
Enthalpies of mixing and excess heat capacities of dilute solutions of n-decanol with n-heptane and n-tridecane, Bull. Acad. Pol. Sci.,
Ser. Sci. Chim., 1975, 23, 759-764. [all data]
Davies and Kybett, 1965
Davies, M.; Kybett, B.,
Sublimation and vaporization heats of long-chain alcohols,
Trans. Faraday Soc., 1965, 61, 1608. [all data]
Costello and Bowden, 1958
Costello, J.M.; Bowden, S.T.,
The Temperature Variation of Orthobaric Density Difference in Liquid-Vapor Systems III. Alcohols,
Recl. Trav. Chim. Pays-Bas, 1958, 77, 36-46. [all data]
Badin, 1943
Badin, E.J.,
J. Am. Chem. Soc., 1943, 65, 1809. [all data]
Spizzichino, 1956
Spizzichino, C.,
Contribution a l'etude des tensions de vapeur et des chaleurs de vaporisation des acides gras, esters methyliques et alcools gras a des pressions inferieures a 1 mm de mercure,
J. des Recherches du C.N.R.S., 1956, 34, 1-24. [all data]
Gude and Teja, 1995
Gude, M.; Teja, A.S.,
Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols,
J. Chem. Eng. Data, 1995, 40, 1025-1036. [all data]
Quadri, Khilar, et al., 1991
Quadri, S.K.; Khilar, K.C.; Kudchadker, A.P.; Patni, M.J.,
Measurement of the critical temperatures and critical pressures of some thermally stable or mildly unstable alkanols,
J. Chem. Thermodyn., 1991, 23, 67-76. [all data]
Rosenthal and Teja, 1990
Rosenthal, D.J.; Teja, A.S.,
The Critical Pressures and temperatures of Isomeric Alkanols,
Ind. Eng. Chem. to be published 1990 1990, 1990. [all data]
Rosenthal and Teja, 1989
Rosenthal, D.J.; Teja, A.S.,
Critical pressures and temperatures of isomeric alkanols,
Ind. Eng. Chem. Res., 1989, 28, 1693. [all data]
Teja, Lee, et al., 1989
Teja, A.S.; Lee, R.J.; Rosenthal, D.J.; Anselme, M.J.,
Correlation of the Critical Properties of Alkanes and Alkanols
in 5th IUPAC Conference on Alkanes and AlkanolsGradisca, 1989. [all data]
Anselme and Teja, 1988
Anselme, M.J.; Teja, A.S.,
Critical Temperatures and Densities of Isomeric Alkanols with Six to Ten Carbon Atoms,
Fluid Phase Equilib., 1988, 40, 127-34. [all data]
Efremov, 1966
Efremov, Yu.V.,
Density, Surface Tension, Saturated Vapor Pressurs and Critical Parameters of Alcohols,
Zh. Fiz. Khim., 1966, 40, 1240. [all data]
Karnes, Kybett, et al., 1965
Karnes, H.A.; Kybett, B.D.; Wilson, M.H.; Margrave, J.L.; Newman, M.S.,
Strain energies in hydrocarbons from heats of combustion. III. 3,4,5,6- and 2,4,5,7-tetramethylphenanthrenes,
J. Am. Chem. Soc., 1965, 87, 5554-5558. [all data]
Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]
Kulikov, Verevkin, et al., 2001
Kulikov, Dmitry; Verevkin, Sergey P.; Heintz, Andreas,
Enthalpies of vaporization of a series of aliphatic alcohols,
Fluid Phase Equilibria, 2001, 192, 1-2, 187-207, https://doi.org/10.1016/S0378-3812(01)00633-1
. [all data]
N'Guimbi, Berro, et al., 1999
N'Guimbi, J.; Berro, C.; Mokbel, I.; Rauzy, E.; Jose, J.,
Experimental vapour pressures of 13 secondary and tertiary alcohols---correlation and prediction by a group contribution method,
Fluid Phase Equilibria, 1999, 162, 1-2, 143-158, https://doi.org/10.1016/S0378-3812(99)00168-5
. [all data]
N'Guimbi, Kasehgari, et al., 1992
N'Guimbi, J.; Kasehgari, H.; Mokbel, I.; Jose, J.,
Tensions de vapeur d'alcools primaires dans le domaine 0,3 Pa à 1,5 kPa,
Thermochimica Acta, 1992, 196, 2, 367-377, https://doi.org/10.1016/0040-6031(92)80100-B
. [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]
Wilhoit and Zwolinski, 1973
Wilhoit, R.C.; Zwolinski, B.J.,
Physical and thermodynamic properties of aliphatic alcohols,
J. Phys. Chem. Ref. Data Suppl., 1973, 1, 2, 1. [all data]
Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I.,
Vapor pressure of primary n-alkyl chlorides and alcohols,
J. Chem. Eng. Data, 1969, 14, 1, 98-102, https://doi.org/10.1021/je60040a011
. [all data]
Rose, Papahronis, et al., 1958
Rose, Arthur; Papahronis, B.; Williams, E.,
Experimental Measurement of Vapor-Liquid Equilibria for Octanol-Decanol and Decanol-Dodecanol Binaries.,
Ind. Eng. Chem. Chem. Eng. Data Series, 1958, 3, 2, 216-219, https://doi.org/10.1021/i460004a008
. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Ambrose, Ellender, et al., 1974
Ambrose, D.; Ellender, J.H.; Sprake, C.H.S.,
Thermodynamic properties of organic oxygen compounds XXXV. Vapour pressures of aliphatic alcohols,
The Journal of Chemical Thermodynamics, 1974, 6, 9, 909-914, https://doi.org/10.1016/0021-9614(74)90235-3
. [all data]
Ambrose and Sprake, 1970
Ambrose, D.; Sprake, C.H.S.,
Thermodynamic properties of organic oxygen compounds XXV. Vapour pressures and normal boiling temperatures of aliphatic alcohols,
The Journal of Chemical Thermodynamics, 1970, 2, 5, 631-645, https://doi.org/10.1016/0021-9614(70)90038-8
. [all data]
van Miltenburg, Gabrielová, et al., 2003
van Miltenburg, J. Cees; Gabrielová, Hana; Ruzicka, Kvetoslav,
Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K,
J. Chem. Eng. Data, 2003, 48, 5, 1323-1331, https://doi.org/10.1021/je0340856
. [all data]
Domanska and Gonzalez, 1997
Domanska, U.; Gonzalez, J.A.,
Solid-liquid equilibria for systems containing long-chain 1-alkanols III. Experimental data for 1-tetradecanol, 1-hexadecanol, 1-octadecanol or 1-icosanol + 1-butanol, 1-hexanol, 1-octanol or 1-decanol mixtures. Characterization in terms of DISQUAC,
Fluid Phase Equilibria, 1997, 129, 1-2, 139-163, https://doi.org/10.1016/S0378-3812(96)03150-0
. [all data]
Haas and Harrison, 1993
Haas, M.J.; Harrison, A.G.,
The Fragmentation of Proton-Bound Cluster Ions and the Gas-Phase Acidities of Alcohols,
Int. J. Mass Spectrom. Ion Proc., 1993, 124, 2, 115, https://doi.org/10.1016/0168-1176(93)80003-W
. [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 Pc Critical pressure Ptriple Triple point pressure 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°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔsubH Enthalpy of sublimation ΔsubH° Enthalpy of sublimation at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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