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
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Phase change data
Go To: Top, 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:
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 |
References
Go To: Top, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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]
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]
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]
Notes
Go To: Top, Phase change data, References
- Symbols used in this document:
Pc Critical pressure Ptriple Triple point pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔfusH Enthalpy of fusion 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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