Ethane, nitro-

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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
Δfliquid-144. ± 0.4kJ/molCcbLebedeva and Ryadenko, 1973ALS
Δfliquid-143.6 ± 1.1kJ/molCcbCass, Fletcher, et al., 1958Reanalyzed by Cox and Pilcher, 1970, Original value = -135. ± 1. kJ/mol; ALS
Δfliquid-140.1 ± 1.3kJ/molCcbHolcomb and Dorsey, 1949ALS
Quantity Value Units Method Reference Comment
Δcliquid-1358. ± 0.4kJ/molCcbLebedeva and Ryadenko, 1973ALS
Δcliquid-1358.0 ± 1.0kJ/molCcbCass, Fletcher, et al., 1958Reanalyzed by Cox and Pilcher, 1970, Original value = -1366. ± 1. kJ/mol; ALS
Δcliquid-1361.6 ± 1.3kJ/molCcbHolcomb and Dorsey, 1949ALS

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
134.22298.15Liu and Ziegler, 1966T = 80 to 300 K.; 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil387.6 ± 0.8KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus183.63KN/AToops, 1956Uncertainty assigned by TRC = 0.05 K; TRC
Quantity Value Units Method Reference Comment
Ttriple183.69KN/ALiu and Ziegler, 1966Uncertainty assigned by TRC = 0.04 K; based on analysis of melting curve; TRC
Quantity Value Units Method Reference Comment
Δvap41.6 ± 0.42kJ/molVHolcomb and Dorsey, 1949ALS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
38.6339.EBStephenson and Malanowski, 1987Based on data from 324. to 388. K. See also Toops, 1956, 2 and Dykyj, 1970.; AC
41.3267.N/AStull, 1947Based on data from 252. to 387. K.; AC

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (bar)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
390.0 to 459.1.74671207.774-269.20Tolstova, Kogan, et al., 1965Coefficents calculated by NIST from author's data.
252. to 387.4.712671671.266-31.963Stull, 1947Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
9.853183.69Liu and Ziegler, 1966DH
9.85183.7Domalski and Hearing, 1996AC

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
53.64183.69Liu and Ziegler, 1966DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias

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

C2H4NO2- + Hydrogen cation = Ethane, nitro-

By formula: C2H4NO2- + H+ = C2H5NO2

Quantity Value Units Method Reference Comment
Δr1489. ± 9.2kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1496. ± 12.kJ/molG+TSCumming and Kebarle, 1978gas phase; B
Quantity Value Units Method Reference Comment
Δr1462. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1469. ± 8.4kJ/molIMRECumming and Kebarle, 1978gas phase; B

CAS Reg. No. 34533-65-8 + 2Ethane, nitro- = C6H15N3O6-

By formula: CAS Reg. No. 34533-65-8 + 2C2H5NO2 = C6H15N3O6-

Quantity Value Units Method Reference Comment
Δr61.09 ± 0.84kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr26.4kJ/molTDAsWincel, 2004gas phase; B

Nitrogen oxide anion + Ethane, nitro- = C2H5N2O4-

By formula: NO2- + C2H5NO2 = C2H5N2O4-

Quantity Value Units Method Reference Comment
Δr66.1 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr37.2kJ/molTDAsWincel, 2004gas phase; B

C2H5N2O4- + 2Ethane, nitro- = C4H10N3O6-

By formula: C2H5N2O4- + 2C2H5NO2 = C4H10N3O6-

Quantity Value Units Method Reference Comment
Δr62.3 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr28.5kJ/molTDAsWincel, 2004gas phase; B

C4H10N3O6- + 3Ethane, nitro- = C6H15N4O8-

By formula: C4H10N3O6- + 3C2H5NO2 = C6H15N4O8-

Quantity Value Units Method Reference Comment
Δr49.4 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr16.7kJ/molTDAsWincel, 2004gas phase; B

C6H15N4O8- + 4Ethane, nitro- = C8H20N5O10-

By formula: C6H15N4O8- + 4C2H5NO2 = C8H20N5O10-

Quantity Value Units Method Reference Comment
Δr46.0 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr11.3kJ/molTDAsWincel, 2004gas phase; B

C6H15N3O6- + 3Ethane, nitro- = C8H20N4O8-

By formula: C6H15N3O6- + 3C2H5NO2 = C8H20N4O8-

Quantity Value Units Method Reference Comment
Δr56.9 ± 1.3kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr19.7kJ/molTDAsWincel, 2004gas phase; B

C8H20N4O8- + 4Ethane, nitro- = C10H25N5O10-

By formula: C8H20N4O8- + 4C2H5NO2 = C10H25N5O10-

Quantity Value Units Method Reference Comment
Δr49.8 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr8.79kJ/molTDAsWincel, 2004gas phase; B

C4H10N2O6- + 2Ethane, nitro- = C6H15N3O8-

By formula: C4H10N2O6- + 2C2H5NO2 = C6H15N3O8-

Quantity Value Units Method Reference Comment
Δr53.1 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr18.4kJ/molTDAsWincel, 2004gas phase; B

C6H15N3O8- + 3Ethane, nitro- = C8H20N4O10-

By formula: C6H15N3O8- + 3C2H5NO2 = C8H20N4O10-

Quantity Value Units Method Reference Comment
Δr47.3 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr10.0kJ/molTDAsWincel, 2004gas phase; B

C8H20N4O10- + 4Ethane, nitro- = C10H25N5O12-

By formula: C8H20N4O10- + 4C2H5NO2 = C10H25N5O12-

Quantity Value Units Method Reference Comment
Δr43.9 ± 2.1kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr2.9kJ/molTDAsWincel, 2004gas phase; B

C4H8N2O4- + 2Ethane, nitro- = C6H13N3O6-

By formula: C4H8N2O4- + 2C2H5NO2 = C6H13N3O6-

Quantity Value Units Method Reference Comment
Δr63.6 ± 3.3kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr23.8kJ/molTDAsWincel, 2004gas phase; B

C4H9N2O4- + 2Ethane, nitro- = C6H14N3O6-

By formula: C4H9N2O4- + 2C2H5NO2 = C6H14N3O6-

Quantity Value Units Method Reference Comment
Δr64.4 ± 3.3kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr25.9kJ/molTDAsWincel, 2004gas phase; B

C2H3NO2- + Ethane, nitro- = C4H8N2O4-

By formula: C2H3NO2- + C2H5NO2 = C4H8N2O4-

Quantity Value Units Method Reference Comment
Δr65.7 ± 3.3kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr35.6kJ/molTDAsWincel, 2004gas phase; B

C2H4NO2- + Ethane, nitro- = C4H9N2O4-

By formula: C2H4NO2- + C2H5NO2 = C4H9N2O4-

Quantity Value Units Method Reference Comment
Δr67.8 ± 3.3kJ/molTDAsWincel, 2004gas phase; B
Quantity Value Units Method Reference Comment
Δr37.7kJ/molTDAsWincel, 2004gas phase; B

C2H6NO2+ + Ethane, nitro- = (C2H6NO2+ • Ethane, nitro-)

By formula: C2H6NO2+ + C2H5NO2 = (C2H6NO2+ • C2H5NO2)

Quantity Value Units Method Reference Comment
Δr130.kJ/molPHPMSMeot-Ner, Hunter, et al., 1979gas phase; M
Quantity Value Units Method Reference Comment
Δr140.J/mol*KPHPMSMeot-Ner, Hunter, et al., 1979gas phase; M

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) = 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
21. XN/AValue given here as quoted by missing citation.
140. MN/AValue at T = 303. K.
21. VN/A 

IR Spectrum

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Mass spectrum (electron ionization), References, Notes

Data compiled by: Coblentz Society, Inc.

Data compiled by: Tanya L. Myers, Russell G. Tonkyn, Ashley M. Oeck, Tyler O. Danby, John S. Loring, Matthew S. Taubman, Stephen W. Sharpe, Jerome C. Birnbaum, and Timothy J. Johnson

Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director


Mass spectrum (electron ionization)

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, 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: NIST Mass Spectrometry Data Center, William E. Wallace, director

Spectrum

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Mass spectrum
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Additional Data

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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 Japan AIST/NIMC Database- Spectrum MS-NW- 669
NIST MS number 227638

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References

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), Notes

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

Lebedeva and Ryadenko, 1973
Lebedeva, N.D.; Ryadenko, V.L.R., Enthalpies of formation of nitroalkanes, Russ. J. Phys. Chem. (Engl. Transl.), 1973, 47, 1382. [all data]

Cass, Fletcher, et al., 1958
Cass, R.C.; Fletcher, S.E.; Mortimer, C.T.; Quincey, P.G.; Springall, H.D., Heats of combustion and molecular structure. Part IV. Aliphatic nitroalkanes and nitric esters, J. Chem. Soc., 1958, 958-962. [all data]

Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G., Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]

Holcomb and Dorsey, 1949
Holcomb, D.E.; Dorsey, C.L., Jr., Thermodynamic properties of nitroparaffins, Ind. Eng. Chem., 1949, 41, 2788-2792. [all data]

Liu and Ziegler, 1966
Liu, K.F.; Ziegler, W.T., Heat capacity from 80° to 300°K., melting point and heat of fusion of nitroethane, J. Chem. Eng. Data, 1966, 11, 187-189. [all data]

Toops, 1956
Toops, E.E., Physical Properties of High Purity Nitroparaffins, J. Phys. Chem., 1956, 60, 304-6. [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]

Toops, 1956, 2
Toops, Emory E., Physical Properties of Eight High-Purity Nitroparaffins, J. Phys. Chem., 1956, 60, 3, 304-306, https://doi.org/10.1021/j150537a012 . [all data]

Dykyj, 1970
Dykyj, J., Petrochemica, 1970, 10, 2, 51. [all data]

Stull, 1947
Stull, Daniel R., Vapor Pressure of Pure Substances. Organic and Inorganic Compounds, Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022 . [all data]

Tolstova, Kogan, et al., 1965
Tolstova, T.S.; Kogan, V.B.; Skorokhodova, V.L., Equilibrium Liquid-Steam in Systems Nitrobensol-Nitromethane, Nitrobensol-Nitroethane, Zh. Prikl. Khim. (Leningrad), 1965, 38, 11, 2617-2618. [all data]

Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D., Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III, J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985 . [all data]

Bartmess, Scott, et al., 1979
Bartmess, J.E.; Scott, J.A.; McIver, R.T., Jr., The gas phase acidity scale from methanol to phenol, J. Am. Chem. Soc., 1979, 101, 6047. [all data]

Cumming and Kebarle, 1978
Cumming, J.B.; Kebarle, P., Summary of gas phase measurements involving acids AH. Entropy changes in proton transfer reactions involving negative ions. Bond dissociation energies D(A-H) and electron affinities EA(A), Can. J. Chem., 1978, 56, 1. [all data]

Wincel, 2004
Wincel, H., Gas-phase clustering reactions of NO2-, C2H3NO2-, C2H4NO2-C2H5NO2- and C2H5NO4- with C2H5NO2, Int. J. Mass Spectrom., 2004, 232, 2, 185-194, https://doi.org/10.1016/j.ijms.2004.01.003 . [all data]

Meot-Ner, Hunter, et al., 1979
Meot-Ner, (Mautner); Hunter, E.P.; Field, F.H., Ion Thermochemistry of Low Volatility Compounds in the Gas Phase. I. Intrinsic Basicities of Alpha - Amino Acids, J. Am. Chem. Soc., 1979, 101, 3, 686, https://doi.org/10.1021/ja00497a034 . [all data]


Notes

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), References