Cyclohexane, methyl-

InChI version 1.06

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Gas phase thermochemistry data

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.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-154.8 ± 1.0kJ/molCcbProsen, Johnson, et al., 1946ALS
Δfgas-159.9kJ/molN/AMoore, Renquist, et al., 1940Value computed using ΔfHliquid° value of -195.3±1.9 kj/mol from Moore, Renquist, et al., 1940 and ΔvapH° value of 35.4 kj/mol from Prosen, Johnson, et al., 1946.; DRB
Quantity Value Units Method Reference Comment
gas343.30J/mol*KN/ABeckett C.W., 1947GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
36.5050.Thermodynamics Research Center, 1997p=1 bar. Recommended S(T) and Cp(T) values differ significantly from earlier statistically calculated values [ Beckett C.W., 1947] at high temperatures (6 and 7 J/mol*K, respectively, at 1500 K).; GT
52.01100.
70.55150.
90.31200.
123.5273.15
135.8298.15
136.7300.
186.0400.
229.9500.
266.8600.
297.6700.
323.5800.
345.4900.
364.11000.
380.11100.
393.81200.
405.61300.
415.81400.
424.51500.
441.81750.
454.22000.
463.32250.
470.12500.
475.42750.
479.53000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
180.75390.Spitzer R., 1946Please also see Montgomery J.B., 1942.; GT
184.6 ± 1.7398.
189.12410.
203.4 ± 2.1439.
222.8 ± 2.1480.
241.9 ± 2.5527.

Condensed phase thermochemistry data

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
Δfliquid-190.2 ± 1.0kJ/molCcbProsen, Johnson, et al., 1946ALS
Δfliquid-195.3 ± 1.9kJ/molCcbMoore, Renquist, et al., 1940Reanalyzed by Cox and Pilcher, 1970, Original value = -192.5 kJ/mol; ALS
Quantity Value Units Method Reference Comment
Δcliquid-4565.29 ± 0.96kJ/molCcbProsen, Johnson, et al., 1946Corresponding Δfliquid = -190.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-4564.3 ± 1.9kJ/molCcbMoore, Renquist, et al., 1940Reanalyzed by Cox and Pilcher, 1970, Original value = -4562.3 ± 1.9 kJ/mol; Corresponding Δfliquid = -191.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-4604.9kJ/molCcbZubova, 1901Corresponding Δfliquid = -151. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid247.90J/mol*KN/ADouslin and Huffman, 1946DH
liquid248.1J/mol*KN/AParks and Huffman, 1930Extrapolation below 90 K, 54.73 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
184.38298.15Shiohama, Ogawa, et al., 1988DH
184.96298.15Tanaka, 1985DH
185.29298.15Grolier, Inglese, et al., 1982T = 298.15 K.; DH
184.8298.15Wilhelm, Grolier, et al., 1979DH
184.84298.15Holzhauer and Ziegler, 1975T = 144 to 312 K. Cp = 129.88277 - 0.0054107773T + 7.9975642x10-4T2 J/mol*K.; DH
185.27298.055Hwa and Ziegler, 1966T = 175 to 308 K. Unsmoothed experimental datum.; DH
184.51298.15Douslin and Huffman, 1946T = 12 to 300 K.; DH
182.0294.2Parks and Huffman, 1930T = 93 to 294 K. Value is unsmoothed experimental datum.; DH

Phase change data

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
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.

Quantity Value Units Method Reference Comment
Tboil374.0 ± 0.8KAVGN/AAverage of 101 out of 106 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus146.6 ± 0.4KAVGN/AAverage of 15 out of 16 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple146.58KN/ADouslin and Huffman, 1946, 2Uncertainty assigned by TRC = 0.05 K; To = 273.16 K; TRC
Ttriple146.57KN/ADouslin and Huffman, 1946, 2Uncertainty assigned by TRC = 0.08 K; To = 273.16 K; TRC
Quantity Value Units Method Reference Comment
Tc573. ± 2.KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Pc34.8 ± 0.2barN/ADaubert, 1996
Pc34.71barN/AKudchadker, Alani, et al., 1968Uncertainty assigned by TRC = 0.304 bar; TRC
Pc34.7768barN/AKay, 1947Uncertainty assigned by TRC = 0.0506 bar; TRC
Quantity Value Units Method Reference Comment
Vc0.369l/molN/ADaubert, 1996
Quantity Value Units Method Reference Comment
ρc2.71 ± 0.02mol/lN/ADaubert, 1996
ρc2.719mol/lN/AKudchadker, Alani, et al., 1968Uncertainty assigned by TRC = 0.03 mol/l; TRC
ρc2.715mol/lN/ASimon, 1957Uncertainty assigned by TRC = 0.03 mol/l; TRC
ρc2.71mol/lN/AKay, 1947Uncertainty assigned by TRC = 0.02 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap35.3 ± 0.2kJ/molAVGN/AAverage of 10 out of 11 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
31.27374.1N/AMajer and Svoboda, 1985
33.8340.N/ASapei, Uusi-Kyyny, et al., 2010Based on data from 325. to 374. K.; AC
36.2310.N/AWu, Pividal, et al., 1991Based on data from 295. to 333. K.; AC
32.3388.AStephenson and Malanowski, 1987Based on data from 373. to 511. K.; AC
31.2516.AStephenson and Malanowski, 1987Based on data from 501. to 573. K.; AC
34.6323.AStephenson and Malanowski, 1987Based on data from 308. to 368. K. See also Valerga, 1970 and Boublik, Fried, et al., 1984.; AC
32.2353.N/AEubank, Cediel, et al., 1984AC
29.9393.N/AEubank, Cediel, et al., 1984AC
26.9433.N/AEubank, Cediel, et al., 1984AC
23.4473.N/AEubank, Cediel, et al., 1984AC
34.6 ± 0.1313.CMajer, Svoboda, et al., 1979AC
33.5 ± 0.1333.CMajer, Svoboda, et al., 1979AC
32.5 ± 0.1353.CMajer, Svoboda, et al., 1979AC
31.8374.N/ASpitzer and Pitzer, 1946AC
34.9314.MMWillingham, Taylor, et al., 1945Based on data from 299. to 375. K.; AC
36.1288.N/AStuckey and Saylor, 1940Based on data from 273. to 348. 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)

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Temperature (K) A (kJ/mol) β Tc (K) Reference Comment
298. to 374.49.560.2685572.1Majer and Svoboda, 1985

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
6.7505146.58Douslin and Huffman, 1946DH
6.69146.6Domalski and Hearing, 1996AC
6.673146.2Parks and Huffman, 1930DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
46.05146.58Douslin and Huffman, 1946DH
45.14146.2Parks and Huffman, 1930DH

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Reaction thermochemistry data

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

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Individual Reactions

Quantity Value Units Method Reference Comment
Δr-119.5 ± 0.65kJ/molChydRogers, Crooks, et al., 1987liquid phase
Δr-116.1 ± 0.54kJ/molChydTurner and Garner, 1958liquid phase; solvent: Acetic acid
Δr-116.1 ± 0.54kJ/molEqkTurner and Garner, 1957liquid phase; solvent: Acetic acid
Δr-120.1 ± 0.3kJ/molChydTurner and Garner, 1957, 2liquid phase; solvent: Acetic acid
Quantity Value Units Method Reference Comment
Δr-111.4 ± 0.37kJ/molChydRogers, Crooks, et al., 1987liquid phase
Δr-106.3 ± 0.46kJ/molChydTurner and Garner, 1958liquid phase; solvent: Acetic acid
Δr-106.3 ± 0.46kJ/molChydTurner and Garner, 1957liquid phase; solvent: Acetic acid
Quantity Value Units Method Reference Comment
Δr-387. ± 0.4kJ/molChydRoth, Adamczak, et al., 1991liquid phase

Henry's Law data

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) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
0.00979400.MN/A
0.00939100.XN/A
0.0023 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
0.0025 LN/A
0.0023 VN/A

Gas phase ion energetics data

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
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron

Quantity Value Units Method Reference Comment
IE (evaluated)9.64 ± 0.10eVN/AN/AL

Ionization energy determinations

IE (eV) Method Reference Comment
9.62 ± 0.05EIHolmes and Lossing, 1991LL
9.64EQSieck and Mautner(Meot-Ner), 1982LBLHLM
9.64 ± 0.10EVALLias, 1982LBLHLM
9.69 ± 0.15EQMautner(Meot-Ner), Sieck, et al., 1981LLK
9.76 ± 0.03PERang, Paldoia, et al., 1974LLK
9.85 ± 0.03PIWatanabe, Nakayama, et al., 1962RDSH

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
C6H11 + 10.95CH3EIPottie, Harrison, et al., 1961RDSH

IR Spectrum

Data compiled by: Coblentz Society, Inc.

Mass spectrum (electron ionization)

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Spectrum

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