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
- Permanent link for this species. Use this link for bookmarking this species for future reference.
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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:
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
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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
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 |
Reaction 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 by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: H2 + C10H20 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -29.69 ± 0.29 | kcal/mol | Chyd | Rogers and Skanupong, 1974 | liquid phase; solvent: Hexane |
ΔrH° | -29.89 ± 0.31 | kcal/mol | Chyd | Bretschneider and Rogers, 1970 | liquid phase; solvent: galcial acetic acid |
By formula: 3H2 + C10H16 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -95.6 ± 0.5 | kcal/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid |
By formula: 3H2 + C10H16 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -95.9 ± 0.2 | kcal/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid |
By formula: H2 + C10H20 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28.56 ± 0.35 | kcal/mol | Chyd | Rogers and Siddiqui, 1975 | liquid phase; solvent: n-Hexane |
By formula: 2H2 + C10H18 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.27 ± 0.51 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane |
By formula: 2H2 + C10H18 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -64.86 ± 0.47 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane |
By formula: 2H2 + C10H18 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -64.39 ± 0.41 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane |
By formula: 2H2 + C10H18 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -64.10 ± 0.47 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane |
By formula: 2H2 + C10H18 = C10H22
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -69.65 ± 0.51 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane |
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 |
---|---|---|---|---|
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
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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 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 |
IR Spectrum
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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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Gas Phase Spectrum
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Additional Data
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Owner | NIST Standard Reference Data Program Collection (C) 2018 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | Sadtler Research Labs Under US-EPA Contract |
State | gas |
Mass spectrum (electron ionization)
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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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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Due to licensing restrictions, this spectrum cannot be downloaded.
Owner | NIST Mass Spectrometry Data Center Collection (C) 2014 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | NIST Mass Spectrometry Data Center, 1990. |
NIST MS number | 114147 |
Gas Chromatography
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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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Lee's RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-5MS | 159.66 | Chen, Keeran, et al., 2002 | 30. m/0.25 mm/0.5 μm, 40. C @ 1. min, 10. K/min; Tend: 310. C |
Capillary | DB-5MS | 163.22 | Chen, Keeran, et al., 2002 | 30. m/0.25 mm/0.5 μm, 40. C @ 1. min, 4. K/min; Tend: 310. C |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), Gas Chromatography, Site Links, NIST Free Links, NIST Subscription Links, 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,
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Notes
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- 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 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 ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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