Decane
- Formula: C10H22
- Molecular weight: 142.2817
- IUPAC Standard InChIKey: DIOQZVSQGTUSAI-UHFFFAOYSA-N
- CAS Registry Number: 124-18-5
- 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: n-Decane; n-C10H22; UN 2247
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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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -59.67 ± 0.26 | kcal/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 130.46 ± 0.26 | cal/mol*K | N/A | Scott D.W., 1974 | This reference does not contain the original experimental data. Experimental entropy value is based on the results [ Messerly J.F., 1967] for S(liquid).; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
42.801 | 200. | Scott D.W., 1974, 2 | Recommended values were obtained from the consistent correlation scheme for alkanes [ Scott D.W., 1974, Scott D.W., 1974, 2]. This approach gives a good agreement with experimental data available for alkanes. However, large uncertainties could be expected at high temperatures.; GT |
52.079 | 273.15 | ||
55.7 ± 0.1 | 298.15 | ||
55.970 | 300. | ||
71.219 | 400. | ||
85.189 | 500. | ||
97.000 | 600. | ||
106.70 | 700. | ||
114.70 | 800. | ||
121.50 | 900. | ||
127.10 | 1000. | ||
131.90 | 1100. | ||
136.10 | 1200. | ||
140.00 | 1300. | ||
143.00 | 1400. | ||
146.00 | 1500. |
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 | -71.95 ± 0.26 | kcal/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1620.06 ± 0.21 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Corresponding ΔfHºliquid = -71.92 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1620.13 ± 0.36 | kcal/mol | Ccb | Prosen and Rossini, 1944 | Corresponding ΔfHºliquid = -71.85 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1619.1 | kcal/mol | Ccb | Jessup, 1937 | Corresponding ΔfHºliquid = -72.90 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 101.79 | cal/mol*K | N/A | Finke, Gross, et al., 1954 | DH |
S°liquid | 102.5 | cal/mol*K | N/A | Huffman, Parks, et al., 1931 | Extrapolation below 90 K, 92.05 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
75.155 | 298.9 | Czarnota, 1993 | p = 0.1 MPa.; DH |
77.407 | 318.15 | Banipal, Garg, et al., 1991 | T = 313 to 373 K. p = 0.1 MPa.; DH |
75.397 | 298.15 | Trejo, Costas, et al., 1991 | DH |
75.397 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
75.363 | 298.15 | Costas, Huu, et al., 1988 | DH |
75.29 | 298.23 | Kuznetsov, Kharin, et al., 1988 | T = 293 to 420 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.214 kJ/kg*K.; DH |
74.919 | 298.15 | Perez-Casas, Aicart, et al., 1988 | DH |
74.840 | 298.15 | Pintos, Bravo, et al., 1988 | DH |
75.397 | 298.15 | Wilhelm, Inglese, et al., 1987 | DH |
74.943 | 298.15 | Gates, Wood, et al., 1986 | T = 298.15 to 368.15 K.; DH |
75.397 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
74.866 | 298.15 | Baluja, Bravo, et al., 1985 | DH |
75.244 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
74.806 | 298.15 | Lainez, Rodrigo, et al., 1985 | DH |
74.830 | 298.15 | Lainez, Roux-Desgranges, et al., 1985 | DH |
74.830 | 298.15 | Lainez, Wilhelm, et al., 1985 | DH |
75.031 | 298.15 | Grolier, Inglese, et al., 1984 | DH |
75.098 | 298.15 | Roux, Grolier, et al., 1984 | DH |
74.154 | 293.15 | Siddiqi, Svejda, et al., 1983 | DH |
74.69 | 298.15 | Wilhelm, Inglese, et al., 1982 | DH |
74.76 | 298. | Zaripov, 1982 | T = 298, 323, 363 K.; DH |
74.88 | 298.15 | Grolier, Hamedi, et al., 1979 | DH |
74.50 | 298. | Grigor'ev, Rastorguev, et al., 1975 | T = 300 to 463 K.; DH |
75.160 | 298.15 | Finke, Gross, et al., 1954 | T = 12 to 300 K.; DH |
74.639 | 299.8 | Schlinger and Sage, 1952 | T = 80 to 200°F.; DH |
75.041 | 298.15 | Osborne and Ginnings, 1947 | T = 278 to 318 K.; DH |
74.40 | 297.7 | Huffman, Parks, et al., 1931 | T = 91 to 298 K. Value is unsmoothed experimental datum.; DH |
74.00 | 295.5 | Parks, Huffman, et al., 1930 | T = 242 to 296 K. Value is unsmoothed experimental datum.; 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 447.2 ± 0.3 | K | AVG | N/A | Average of 34 out of 43 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 243.3 ± 0.6 | K | AVG | N/A | Average of 23 out of 25 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 243.4 ± 0.3 | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 617.8 ± 0.7 | K | AVG | N/A | Average of 16 out of 18 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 20.8 ± 0.8 | atm | AVG | N/A | Average of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.624 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 1.60 ± 0.05 | mol/l | N/A | Ambrose and Tsonopoulos, 1995 | |
ρc | 1.67 | mol/l | N/A | Steele, 1992 | Uncertainty assigned by TRC = 0.070 mol/l; TRC |
ρc | 1.60 | mol/l | N/A | Anselme, Gude, et al., 1990 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 1.67 | mol/l | N/A | Knipmeyer, Archer, et al., 1989 | Uncertainty assigned by TRC = 0.070 mol/l; TRC |
ρc | 1.595 | mol/l | N/A | Gehrig and Lentz, 1983 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 12.27 ± 0.07 | kcal/mol | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 19.2 | kcal/mol | B | Swain, Kwan, et al., 1980 | AC |
ΔsubH° | 19.7 | kcal/mol | H | Bondi, 1963 | See also Chickos, Hosseini, et al., 1993.; AC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.261 | 447.3 | N/A | Majer and Svoboda, 1985 | |
11.5 | 339. | GC | Mokbel, Razzouk, et al., 2007 | Based on data from 324. to 402. K.; AC |
11.1 | 352. | N/A | Batiu, 2002 | Based on data from 337. to 376. K.; AC |
12.3 | 299. | C | Viton, Chavret, et al., 1996 | AC |
12.1 | 314. | C | Viton, Chavret, et al., 1996 | AC |
12.0 | 324. | C | Viton, Chavret, et al., 1996 | AC |
11.8 | 334. | C | Viton, Chavret, et al., 1996 | AC |
10.2 | 424. | N/A | Lee, Dempsey, et al., 1992 | Based on data from 409. to 584. K.; AC |
11.5 | 340. | EB,IP | Chirico, Nguyen, et al., 1989 | Based on data from 268. to 490. K.; AC |
12.9 | 267. | A | Stephenson and Malanowski, 1987 | Based on data from 252. to 383. K.; AC |
9.97 | 462. | A | Stephenson and Malanowski, 1987 | Based on data from 447. to 526. K.; AC |
9.23 | 539. | A | Stephenson and Malanowski, 1987 | Based on data from 524. to 617. K.; AC |
10.8 | 388. | N/A | Stephenson and Malanowski, 1987 | Based on data from 373. to 443. K. See also Varushchenko, Belikova, et al., 1970.; AC |
12.0 | 313. | GS | Allemand, Jose, et al., 1986 | Based on data from 298. to 347. K.; AC |
11.9 ± 0.41 | 308. to 351. | N/A | Beckhaus, Ruchardt, et al., 1984 | AC |
13.4 | 258. | N/A | Carruth and Kobayashi, 1973 | Based on data from 243. to 310. K.; AC |
10.9 | 383. | MM | Willingham, Taylor, et al., 1945 | Based on data from 368. to 440. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kcal/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 444. | 17.78 | 0.3238 | 617.4 | Majer and Svoboda, 1985 |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
243.49 to 310.59 | 0.20450 | 440.616 | -156.896 | Carruth and Kobayashi, 1973 | Coefficents calculated by NIST from author's data. |
367.63 to 448.27 | 4.07286 | 1501.268 | -78.67 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
20.3 | 243. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
6.8631 | 243.51 | N/A | Finke, Gross, et al., 1954 | DH |
6.60 | 243. | DSC | Marti, Kaisersberger, et al., 2004 | AC |
6.86 | 243.5 | N/A | Domalski and Hearing, 1996 | AC |
6.8781 | 243.1 | N/A | Huffman, Parks, et al., 1931 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
28.184 | 243.51 | Finke, Gross, et al., 1954 | DH |
28.200 | 243.5 | Domalski and Hearing, 1996 | CAL |
28.30 | 243.1 | Huffman, Parks, et al., 1931 | 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 |
---|---|---|---|---|
0.00021 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.00014 | L | N/A |
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:
L - Sharon G. Lias
Data compiled as indicated in comments:
LL - Sharon G. Lias and Joel F. Liebman
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
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.65 | eV | N/A | N/A | L |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.73 | EST | Luo and Pacey, 1992 | LL |
9.65 ± 0.10 | EVAL | Lias, 1982 | LBLHLM |
9.54 ± 0.15 | EQ | Mautner(Meot-Ner), Sieck, et al., 1981 | LLK |
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.
Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D.,
Heats of combustion and formation of the paraffin hydrocarbons at 25° C,
J. Res. NBS, 1945, 263-267. [all data]
Scott D.W., 1974
Scott D.W.,
Correlation of the chemical thermodynamic properties of alkane hydrocarbons,
J. Chem. Phys., 1974, 60, 3144-3165. [all data]
Messerly J.F., 1967
Messerly J.F.,
Low-temperature thermal data for n-pentane, n-heptadecane, and n-octadecane. Revised thermodynamic functions for the n-alkanes, C5-C18,
J. Chem. Eng. Data, 1967, 12, 338-346. [all data]
Scott D.W., 1974, 2
Scott D.W.,
Chemical Thermodynamic Properties of Hydrocarbons and Related Substances. Properties of the Alkane Hydrocarbons, C1 through C10 in the Ideal Gas State from 0 to 1500 K. U.S. Bureau of Mines, Bulletin 666, 1974. [all data]
Prosen and Rossini, 1944
Prosen, E.J.; Rossini, F.D.,
Heats of combustion of eight normal paraffin hydrocarbons in the liquid state,
J. Res. NBS, 1944, 33, 255-272. [all data]
Jessup, 1937
Jessup, R.S.,
Heats of combustion of the liquid normal paraffin hydrocarbons from hexane to dodecane,
J. Res. NBS, 1937, 18, 114-128. [all data]
Finke, Gross, et al., 1954
Finke, H.L.; Gross, M.E.; Waddington, G.; Huffman, H.M.,
Low-temperature thermal data for the nine normal paraffin hydrocarbons from octane to hexadecane,
J. Am. Chem. Soc., 1954, 76, 333-341. [all data]
Huffman, Parks, et al., 1931
Huffman, H.M.; Parks, G.S.; Barmore, M.,
Thermal data on organic compounds. X. Further studies on the heat capacities, entropies and free energies of hydrocarbons,
J. Am. Chem. Soc., 1931, 53, 3876-3888. [all data]
Czarnota, 1993
Czarnota, I.,
Heat capacity of decane at high pressures,
J. Chem. Thermodynam., 1993, 25, 639-642. [all data]
Banipal, Garg, et al., 1991
Banipal, T.S.; Garg, S.K.; Ahluwalia, J.C.,
Heat capacities and densities of liquid n-octane, n-nonane, n-decane, and n-hexadecane at temperatures from 318.15 to 373.15 K and at pressures up to 10 MPa,
J. Chem. Thermodynam., 1991, 23, 923-931. [all data]
Trejo, Costas, et al., 1991
Trejo, L.M.; Costas, M.; Patterson, D.,
Excess heat capacity of organic mixtures, Internat. DATA Series,
Selected Data Mixt., 1991, Ser. [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]
Costas, Huu, et al., 1988
Costas, M.; Huu, V.T.; Patterson, D.; Caceres-Alonso, M.; Tardajos, G.; Aicart, E.,
Liquid structure and second-order mixing functions for l-chloronaphthalene with linear and branched alkanes, J. Chem. Soc.,
Faraday Trans., 1988, 1 84(5), 1603-1616. [all data]
Kuznetsov, Kharin, et al., 1988
Kuznetsov, M.A.; Kharin, V.E.; Gerasimov, A.A.; Grigor'ev, M.D.,
Isobaric heat capacity of n-alkanes C7 to C10 at temperatures 293 to 630 K and pressures up to 60 MPa, Izv. Vyssh. Ucheb. Zabed.,
Neft i Gaz, 1988, 31(11), 49-52. [all data]
Perez-Casas, Aicart, et al., 1988
Perez-Casas, S.; Aicart, E.; Trojo, L.M.; Costas, M.,
Excess heat capacity. Chlorobenzene-2,2,4,4,6,8,8-heptamethylnonane, Int. Data Ser.,
Sel. Data Mixtures, 1988, (2)A, 123. [all data]
Pintos, Bravo, et al., 1988
Pintos, M.; Bravo, R.; Baluja, M.C.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Can. J. Chem., 1988, 1179. [all data]
Wilhelm, Inglese, et al., 1987
Wilhelm, E.; Inglese, A.; Roux, A.H.; Grolier, J.-P.E.,
Excess enthalpy, excess heat capacity and excess volume of 1,2,4-trimethylbenzene +, and 1-methylnaphthalene + an n-alkane,
Fluid Phase Equilibria, 1987, 34, 49-67. [all data]
Gates, Wood, et al., 1986
Gates, J.A.; Wood, R.H.; Cobos, J.C.; Casanova, C.; Roux, A.H.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Densities and heat capacities of 1-butanol + n-decane from 298 K to 400 K,
Fluid Phase Equilib., 1986, 27, 137-151. [all data]
Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D.,
Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc.,
Faraday Trans., 1986, 1 82, 2977-2987. [all data]
Baluja, Bravo, et al., 1985
Baluja, M.C.; Bravo, R.; Pintos, M.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Unusual dependence on concentration of the excess heat capacities of ester solutions in alkanes,
Calorim. Anal. Therm., 1985, 16, 138-144. [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]
Lainez, Rodrigo, et al., 1985
Lainez, A.; Rodrigo, M.; Roux, A.H.; Grolier, J.-P.E.; Wilhelm, E.,
Relations between structure and thermodynamic properties. Heat capacities of polar substances (nitrobenzene and benzonitrile) in alkane solutions,
Calorim. Anal. Therm., 1985, 16, 153-158. [all data]
Lainez, Roux-Desgranges, et al., 1985
Lainez, A.; Roux-Desgranges, G.; Grolier, J.-P.E.; Wilhelm, E.,
Mixtures of alkanes with polar molecules showing integral rotation: an unusual composition dependence of CpE of 1,2-dichloroethane + an n-alkane,
Fluid Phase Equilib., 1985, 20, 47-56. [all data]
Lainez, Wilhelm, et al., 1985
Lainez, A.; Wilhelm, E.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Excess molar quantities of (a halogenated n-alkane + an n-alkane). A comparative study of mixtures containing either 1-chlorobutane or 1,4-dichlorobutane,
J. Chem. Thermodynam., 1985, 17, 1153-1161. [all data]
Grolier, Inglese, et al., 1984
Grolier, J.-P.E.; Inglese, A.; Wilhelm, E.,
Excess molar heat capacities of (1,4-dioxane + an n-alkane): an unusual composition dependence,
J. Chem. Thermodynam., 1984, 16, 67-71. [all data]
Roux, Grolier, et al., 1984
Roux, A.H.; Grolier, J.-P.E.; Inglese, A.; Wilhelm, E.,
Excess molar enthalpies, excess molar heat capacities and excess molar volumes of (fluorobenzene + an n-alkane),
Ber. Bunsenges. Phys. Chem., 1984, 88, 986-992. [all data]
Siddiqi, Svejda, et al., 1983
Siddiqi, M.A.; Svejda, P.; Kohler, F.,
A generalized van der Waals equation of state II. Excess heat capacities of mixtures containing cycloalkanes (C5,C6), methylcycloalkanes (C5,C6) and n-decane,
Ber. Bunsenges. Phys. Chem., 1983, 87, 1176-1181. [all data]
Wilhelm, Inglese, et al., 1982
Wilhelm, E.; Inglese, A.; Quint, J.R.; Grolier, J.-P.E.,
Molar excess volumes and excess heat capacities of (1,2,4-trichlorobenzene + an alkane),
J. Chem. Thermodynam., 1982, 14, 303-308. [all data]
Zaripov, 1982
Zaripov, Z.I.,
Experimental study of the isobaric heat capacity of liquid organic compounds with molecular weights of up to 4000 a.e.m., 1982, Teplomassoobmen Teplofiz. [all data]
Grolier, Hamedi, et al., 1979
Grolier, J-P.E.; Hamedi, M.H.; Wilhelm, E.; Kehiaian, H.V.,
Excess heat capacities of binary mixtures of carbon tetrachloride with n-alkanes at 298.15 K,
Thermochim. Acta, 1979, 31, 79-84. [all data]
Grigor'ev, Rastorguev, et al., 1975
Grigor'ev, B.A.; Rastorguev, Yu.L.; Yanin, G.S.,
Experimental determination of the isobaric specific heat of n-alkanes,
Iz. Vyssh. Uchebn. Zaved. Neft Gaz 18, 1975, No.10, 63-66. [all data]
Schlinger and Sage, 1952
Schlinger, W.G.; Sage, B.H.,
Isobaric heat capacities at bubble point. cis-2-butene, isopropylbenzene, and n-decane,
Ind. Eng. Chem., 1952, 44, 2454-2456. [all data]
Osborne and Ginnings, 1947
Osborne, N.S.; Ginnings, D.C.,
Measurements of heat of vaporization and heat capacity of a number of hydrocarbons,
J. Res. NBS, 1947, 39, 453-477. [all data]
Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B.,
Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]
Ambrose and Tsonopoulos, 1995
Ambrose, D.; Tsonopoulos, C.,
Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkenes,
J. Chem. Eng. Data, 1995, 40, 531-546. [all data]
Steele, 1992
Steele, W.V.,
Personal Commun. 1992 1992, 1992. [all data]
Anselme, Gude, et al., 1990
Anselme, M.J.; Gude, M.; Teja, A.S.,
The Critical Temperatures and Densities of the n-Alkanes from Pentane to Octadecane,
Fluid Phase Equilib., 1990, 57, 317-26. [all data]
Knipmeyer, Archer, et al., 1989
Knipmeyer, S.E.; Archer, D.G.; Chirico, R.D.; Gammon, B.E.; Hossenlopp, I.A.; Nguyen, A.; Smith, N.K.; Steele, W.V.; Strube, M.M.,
High-temperature enthalpy and critical property measurements using differential scanning calorimeter,
Fluid Phase Equilib., 1989, 52, 185. [all data]
Gehrig and Lentz, 1983
Gehrig, M.; Lentz, H.,
Values of the pressure-molar volume-temperature relationship for n-decane up to 300 MPa and 673 K,
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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,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°gas Entropy of gas at standard conditions 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°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 ΔsubH Enthalpy of sublimation ΔsubH° Enthalpy of sublimation at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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