Naphthalene, decahydro-, cis-
- Formula: C10H18
- Molecular weight: 138.2499
- IUPAC Standard InChIKey: NNBZCPXTIHJBJL-AOOOYVTPSA-N
- CAS Registry Number: 493-01-6
- 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. - Stereoisomers:
- Other names: cis-Bicyclo[4.4.0]Decane; cis-Decahydronaphthalene; cis-Decalin; cis-Perhydronaphthalene; Decahydronaphthalene, (Z)-; c-Decahydronaphthalene; c-Decalin; Decahydronaphthalene, cis; (Z)-Decahydronaphthalene; Bicyclo[4.4.0]decane, isomer # 2; cis-Decahydronapthalene
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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 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 |
---|---|---|---|---|---|
ΔfH°gas | -169.2 ± 2.3 | kJ/mol | Ccb | Speros and Rossini, 1960 | ALS |
ΔfH°gas | -169.6 | kJ/mol | N/A | Davies and Gilbert, 1941 | Value computed using ΔfHliquid° value of -219.9±1.3 kj/mol from Davies and Gilbert, 1941 and ΔvapH° value of 50.3 kj/mol from Speros and Rossini, 1960.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
39.75 | 50. | Dorofeeva O.V., 1988 | Recommended values agree with results of statistical calculations [ Miyazawa T., 1958, Chang S., 1970] within their uncertainties. These functions are also reproduced in the reference book [ Frenkel M., 1994].; GT |
59.89 | 100. | ||
82.98 | 150. | ||
108.15 | 200. | ||
151.73 | 273.15 | ||
168.1 ± 1.0 | 298.15 | ||
169.37 | 300. | ||
236.42 | 400. | ||
297.57 | 500. | ||
349.48 | 600. | ||
392.97 | 700. | ||
429.58 | 800. | ||
460.57 | 900. | ||
486.93 | 1000. | ||
509.43 | 1100. | ||
528.68 | 1200. | ||
545.21 | 1300. | ||
559.44 | 1400. | ||
571.74 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
236.77 | 400. | Miyazawa T., 1958 | GT |
272.00 | 450. |
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 by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -219.5 ± 0.92 | kJ/mol | Ccb | Speros and Rossini, 1960 | |
ΔfH°liquid | -219.9 ± 1.3 | kJ/mol | Ccb | Davies and Gilbert, 1941 | Reanalyzed by Cox and Pilcher, 1970, Original value = -220.7 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -6288.22 ± 0.92 | kJ/mol | Ccb | Speros and Rossini, 1960 | Corresponding ΔfHºliquid = -219.4 kJ/mol (simple calculation by NIST; no Washburn corrections) |
ΔcH°liquid | -6287.7 ± 1.3 | kJ/mol | Ccb | Davies and Gilbert, 1941 | Reanalyzed by Cox and Pilcher, 1970, Original value = -6286.0 ± 0.4 kJ/mol; Corresponding ΔfHºliquid = -219.9 kJ/mol (simple calculation by NIST; no Washburn corrections) |
ΔcH°liquid | -6275.6 | kJ/mol | Ccb | Huckel and Mentzel, 1926 | Corresponding ΔfHºliquid = -232. kJ/mol (simple calculation by NIST; no Washburn corrections) |
ΔcH°liquid | -6280.9 ± 4.1 | kJ/mol | Ccb | Roth and Lasse, 1925 | Corresponding ΔfHºliquid = -226.6 kJ/mol (simple calculation by NIST; no Washburn corrections) |
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
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 466. ± 5. | K | AVG | N/A | Average of 15 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 230. ± 2. | K | AVG | N/A | Average of 12 out of 14 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 230.15 ± 0.09 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 704. ± 3. | K | N/A | Daubert, 1996 | |
Tc | 681. | K | N/A | Matzik and Schneider, 1985 | Uncertainty assigned by TRC = 1.5 K; TRC |
Tc | 705.0 | K | N/A | Pak and Kay, 1972 | Uncertainty assigned by TRC = 1. K; extrapolated to zero time to correct for decomposition; TRC |
Tc | 702.2 | K | N/A | Cheng, McCoubrey, et al., 1962 | Uncertainty assigned by TRC = 1.5 K; extrapolated to zero time to correct for decomposition; calibr. vs NPL thermometer; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 32. ± 2. | bar | N/A | Daubert, 1996 | |
Pc | 24.90 | bar | N/A | Matzik and Schneider, 1985 | Uncertainty assigned by TRC = 0.50 bar; TRC |
Pc | 32.07 | bar | N/A | Pak and Kay, 1972 | Uncertainty assigned by TRC = 0.2068 bar; corrected for vapor pressure of Hg, and extrapolated to zero time to correct for decompostion; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 50.2 ± 2.1 | kJ/mol | V | Speros and Rossini, 1960 | ALS |
ΔvapH° | 50.3 | kJ/mol | N/A | Speros and Rossini, 1960 | DRB |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 62.5 | kJ/mol | H | Bondi, 1963 | See also Chickos, Hosseini, et al., 1993.; AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
45.5 | 386. | A,GS | Stephenson and Malanowski, 1987 | Based on data from 371. to 473. K. See also Camin and Rossini, 1955.; 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 |
---|---|---|---|---|---|
373.03 to 469.53 | 4.00047 | 1594.687 | -69.731 | Camin and Rossini, 1955 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
64.8 | 230. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
14.43 | 242.8 | Domalski and Hearing, 1996 | AC |
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: C10H18 = C10H18
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -11.3 | kJ/mol | Eqk | Nuzzi, 1984 | liquid phase; GC |
ΔrH° | -13.3 | kJ/mol | Eqk | Nuzzi, 1984 | gas phase; GC |
By formula: 5H2 + C10H8 = C10H18
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -318. | kJ/mol | Eqk | Frye and Weitkamp, 1969 | gas phase |
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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Notice: Concentration information is not available for this spectrum and, therefore, molar absorptivity values cannot be derived.
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 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Speros and Rossini, 1960
Speros, D.M.; Rossini, F.D.,
Heats of combustion and formation of naphthalene, the two methylnaphthalenes, cis and trans decahydronaphthalene and related compounds,
J. Phys. Chem., 1960, 64, 1723-1727. [all data]
Davies and Gilbert, 1941
Davies, G.F.; Gilbert, E.C.,
The heat of combustion of cis- and trans-decahydronaphthalene,
J. Am. Chem. Soc., 1941, 63, 1585-1586. [all data]
Dorofeeva O.V., 1988
Dorofeeva O.V.,
Thermodynamic Properties of Polycyclic Aromatic Hydrocarbons in the Gaseous Phase. Institute for High Temperatures, USSR Academy of Sciences, Preprint No.1-238 (in Russian), Moscow, 1988. [all data]
Miyazawa T., 1958
Miyazawa T.,
Thermodynamic functions for gaseous cis- and trans-decalins from 298 to 1000 K,
J. Am. Chem. Soc., 1958, 80, 60-62. [all data]
Chang S., 1970
Chang S.,
The heats of combustion and strain energies of bicyclo[n.m.0]alkanes,
J. Am. Chem. Soc., 1970, 92, 3109-3118. [all data]
Frenkel M., 1994
Frenkel M.,
Thermodynamics of Organic Compounds in the Gas State, Vol. I, II, Thermodynamics Research Center, College Station, Texas, 1994, 1994. [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]
Huckel and Mentzel, 1926
Huckel, W.; Mentzel, R.,
Zur Stereochemie bicyclischer Ringsteme II. Die Stereoisomerie des Dekahydronaphtalins und seiner Derivate II. Stereoisomere β-substituierte Dekaline,
Ann., 1926, 451, 109-132. [all data]
Roth and Lasse, 1925
Roth, W.A.; Lasse, R.,
Verbrennungswarme der Dekahydro-naphthaline und der Dekalone,
Ann., 1925, 441, 48-53. [all data]
Daubert, 1996
Daubert, T.E.,
Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes,
J. Chem. Eng. Data, 1996, 41, 365-372. [all data]
Matzik and Schneider, 1985
Matzik, I.; Schneider, G.M.,
Fluid phase equilibria of binary mixtures of sulfur hexafluoride with octane, nonane, hendecane, and cis-decahydronaphthalene at temperature between 280 K and 440 K and at pressures up to 140 MPa,
Ber. Bunsen-Ges. Phys. Chem., 1985, 89, 551. [all data]
Pak and Kay, 1972
Pak, S.C.; Kay, W.B.,
Gas-Liquid Critical Temperatures of Mixtures. Benzene + n-Alkanes and Hexafluorobenzene + n-Alkanes,
Ind. Eng. Chem. Fundam., 1972, 11, 255. [all data]
Cheng, McCoubrey, et al., 1962
Cheng, D.C.H.; McCoubrey, J.C.; Phillips, D.G.,
Critical Temperatures of Some Organic Cyclic Compounds,
Trans. Faraday Soc., 1962, 58, 224. [all data]
Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
J. Chem. Eng. Data, 1963, 8, 3, 371-381, https://doi.org/10.1021/je60018a027
. [all data]
Chickos, Hosseini, et al., 1993
Chickos, James S.; Hosseini, Sarah; Hesse, Donald G.; Liebman, Joel F.,
Heat capacity corrections to a standard state: a comparison of new and some literature methods for organic liquids and solids,
Struct Chem, 1993, 4, 4, 271-278, https://doi.org/10.1007/BF00673701
. [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]
Camin and Rossini, 1955
Camin, David L.; Rossini, Frederick D.,
Physical Properties of Fourteen API Research Hydrocarbons, C 9 to C 15,
J. Phys. Chem., 1955, 59, 11, 1173-1179, https://doi.org/10.1021/j150533a014
. [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]
Nuzzi, 1984
Nuzzi, M.,
cis-Decalin = trans-decalin reaction. Experimental equilibrium constants and thermodynamic functions of its liquid isomers,
Riv. Combust, 1984, 38, 293-297. [all data]
Frye and Weitkamp, 1969
Frye, C.G.; Weitkamp, A.W.,
Equilibrium hydrogenations of multi-ring aromatics,
J. Chem. Eng. Data, 1969, 14, 372-376. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 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 - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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