Trichloromethane

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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 compiled as indicated in comments:
DRB - Donald R. Burgess, Jr.

Quantity Value Units Method Reference Comment
Δfgas-24.661kcal/molReviewChase, 1998Data last reviewed in December, 1968
Δfgas-24.59 ± 0.60kcal/molReviewManion, 2002derived from recommended ΔfHliquid° and ΔvapH°; DRB
Quantity Value Units Method Reference Comment
gas,1 bar70.652cal/mol*KReviewChase, 1998Data last reviewed in December, 1968

Gas Phase Heat Capacity (Shomate Equation)

Cp° = A + B*t + C*t2 + D*t3 + E/t2
H° − H°298.15= A*t + B*t2/2 + C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 − E/(2*t2) + G
    Cp = heat capacity (cal/mol*K)
    H° = standard enthalpy (kcal/mol)
    S° = standard entropy (cal/mol*K)
    t = temperature (K) / 1000.

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Temperature (K) 298. to 1200.1200. to 6000.
A 10.5753024.25339
B 27.407600.819731
C -21.22810-0.157110
D 6.1902300.010446
E -0.124954-2.234230
F -29.27560-37.23709
G 75.4648992.53241
H -24.65990-24.65990
ReferenceChase, 1998Chase, 1998
Comment Data last reviewed in December, 1968 Data last reviewed in December, 1968

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:
DRB - Donald R. Burgess, Jr.
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-32.05 ± 0.60kcal/molReviewManion, 2002adopted combustion calorimetry data of Hu and Sinke, 1969 with increased uncertainty to reflect other data; DRB
Δfliquid-32.10kcal/molCcrHu and Sinke, 1969, 2ALS
Quantity Value Units Method Reference Comment
Δcliquid-113.10kcal/molCcrHu and Sinke, 1969, 2ALS
Δcliquid-113.3 ± 2.0kcal/molCcbSmith, Bjellerup, et al., 1953Reanalyzed by Cox and Pilcher, 1970, Original value = -113. ± 2. kcal/mol; ALS

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
27.306298.15Grolier, Roux-Desgranges, et al., 1993DH
27.06298.15Shehatta, 1993DH
27.323298.15Barta, Kooner, et al., 1989DH
27.330298.15Barta, Kooner, et al., 1989, 2DH
27.61298.15Petrov, Peshekhodov, et al., 1989T = 258.15, 278.15, 298.15, 318.15 K.; DH
27.211298.15Grolier, Roux-Desgranges, et al., 1987DH
27.61298.15Al'per, Peshekhodov, et al., 1986DH
27.182298.15Hepler, Kooner, et al., 1985DH
27.309298.15Inglese, Castagnolo, et al., 1981DH
27.77293.Rastorguev and Ganiev, 1967T = 293 to 333 K.; DH
27.10300.Harrison and Moelwyn-Hughes, 1957T = 243 to 303 K.; DH
27.25303.2Harrison and Moelwyn-Hughes, 1957T = 245 to 303 K. Unsmoothed experimental datum.; DH
27.290298.Staveley, Tupman, et al., 1955T = 284 to 329 K.; DH
27.99298.Kurbatov, 1948T = -52 to 51°C. Mean Cp, four temperatures.; DH
33.39303.6Phillip, 1939DH
27.01298.1Richards and Wallace, 1932T = 293 to 323 K.; DH
27.61293.2Williams and Daniels, 1925T = 20 to 50°C.; DH
27.89303.Willams and Daniels, 1924T = 295 to 315 K. Equation only.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry 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 compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein

Quantity Value Units Method Reference Comment
Tboil334.3 ± 0.2KAVGN/AAverage of 36 out of 37 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus210. ± 2.KAVGN/AAverage of 14 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple209.61KN/AStull, 1937Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc537. ± 2.KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Pc52.5900atmN/ACampbell and Chatterjee, 1969Uncertainty assigned by TRC = 0.09998 atm; TRC
Pc52.5900atmN/ACampbell and Chatterjee, 1968Uncertainty assigned by TRC = 0.0599 atm; TRC
Quantity Value Units Method Reference Comment
ρc4.11mol/lN/ACampbell and Chatterjee, 1969Uncertainty assigned by TRC = 0.03 mol/l; TRC
ρc3.84mol/lN/ACampbell and Chatterjee, 1968Uncertainty assigned by TRC = 0.02 mol/l; TRC
ρc4.15mol/lN/AHerz and Neukirch, 1923Uncertainty assigned by TRC = 0.02 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap7.50kcal/molN/AMajer and Svoboda, 1985 
Δvap7.49 ± 0.02kcal/molReviewManion, 2002weighted average of several measurements plus a correction for non-ideality; DRB
Δvap7.43kcal/molCMajer, Sváb, et al., 1980AC
Δvap7.30 ± 0.10kcal/molVMathews, 1926Reanalyzed by Pedley, Naylor, et al., 1986, Original value = 7.02 ± 0.05 kcal/mol; ALS

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
6.989334.3N/AMajer and Svoboda, 1985 
7.36321.N/AChen, Wang, et al., 1995Based on data from 306. to 427. K.; AC
7.60254.AStephenson and Malanowski, 1987Based on data from 227. to 269. K.; AC
7.27348.AStephenson and Malanowski, 1987Based on data from 333. to 416. K.; AC
6.91425.AStephenson and Malanowski, 1987Based on data from 410. to 481. K.; AC
7.19494.AStephenson and Malanowski, 1987Based on data from 479. to 523. K.; AC
7.77275.EBBoublík and Aim, 1972Based on data from 260. to 333. K.; AC
8.37230.N/AStull, 1947Based on data from 215. to 334. K.; AC
7.39320.N/AScatchard and Raymond, 1938Based on data from 308. to 333. K.; AC

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
215. to 334.44.202011233.129-40.953Stull, 1947Coefficents calculated by NIST from author's data.
334.4 to 527.4.564211486.455-8.612Stull, 1947Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
2.1209.6Acree, 1991AC

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

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 compiled as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
MS - José A. Martinho Simões
ALS - 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

Chlorine anion + Trichloromethane = (Chlorine anion • Trichloromethane)

By formula: Cl- + CHCl3 = (Cl- • CHCl3)

Quantity Value Units Method Reference Comment
Δr15.2 ± 2.0kcal/molTDAsYamdagni and Kebarle, 1971gas phase; B,M
Δr19.5 ± 2.0kcal/molTDAsHiraoka, Mizuno, et al., 2001gas phase; B
Δr18.10kcal/molMoblGiles and Grimsrud, 1993gas phase; B
Δr18.1 ± 2.0kcal/molIMRELarson and McMahon, 1984gas phase; B,M
Δr19.10 ± 0.70kcal/molTDEqDougherty, Dalton, et al., 1974gas phase; B,M
Quantity Value Units Method Reference Comment
Δr23.2cal/mol*KN/ALarson and McMahon, 1984gas phase; From thermochemical cycle(Cl-)CF3H, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M
Δr24.5cal/mol*KHPMSDougherty, Dalton, et al., 1974gas phase; M
Δr14.8cal/mol*KPHPMSYamdagni and Kebarle, 1971gas phase; Entropy change is questionable; M
Quantity Value Units Method Reference Comment
Δr11. ± 1.kcal/molAVGN/AAverage of 6 values; Individual data points

CCl3- + Hydrogen cation = Trichloromethane

By formula: CCl3- + H+ = CHCl3

Quantity Value Units Method Reference Comment
Δr360.33kcal/molAcidPaulino and Squires, 1991gas phase; B
Δr357.6 ± 2.1kcal/molG+TSPaulino and Squires, 1991gas phase; B
Δr357.0 ± 6.1kcal/molG+TSBohme, Lee-Ruff, et al., 1972gas phase; > acetone, <= C5H6; value altered from reference due to change in acidity scale; B
Quantity Value Units Method Reference Comment
Δr349.9 ± 2.0kcal/molIMRBPaulino and Squires, 1991gas phase; B
Δr349.9 ± 3.0kcal/molIMRBBorn, Ingemann, et al., 2000gas phase; B
Δr349.3 ± 6.0kcal/molIMRBBohme, Lee-Ruff, et al., 1972gas phase; > acetone, <= C5H6; value altered from reference due to change in acidity scale; B

CN- + Trichloromethane = (CN- • Trichloromethane)

By formula: CN- + CHCl3 = (CN- • CHCl3)

Quantity Value Units Method Reference Comment
Δr18.2 ± 3.5kcal/molIMRELarson and McMahon, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr24.8cal/mol*KN/ALarson and McMahon, 1987gas phase; switching reaction,Thermochemical ladder(CN-)H2O, Entropy change calculated or estimated; Payzant, Yamdagni, et al., 1971; M
Quantity Value Units Method Reference Comment
Δr10.8 ± 2.3kcal/molIMRELarson and McMahon, 1987gas phase; B,M

C8H6MoO3 (solution) + Carbon Tetrachloride (solution) = Molybdenum, tricarbonylchloro(η5-2,4-cyclopentadien-1-yl)- (solution) + Trichloromethane (solution)

By formula: C8H6MoO3 (solution) + CCl4 (solution) = C8H5ClMoO3 (solution) + CHCl3 (solution)

Quantity Value Units Method Reference Comment
Δr-31.81 ± 0.91kcal/molRSCNolan, López de la Vega, et al., 1986solvent: Tetrahydrofuran; The enthalpy of solution of Mo(Cp)(CO)3(H)(cr) was measured as 2.1 ± 0.1 kcal/mol Nolan, López de la Vega, et al., 1986, 2. Reaction temperature: 323 K; MS

Bromine anion + Trichloromethane = (Bromine anion • Trichloromethane)

By formula: Br- + CHCl3 = (Br- • CHCl3)

Quantity Value Units Method Reference Comment
Δr15.80kcal/molMoblGiles and Grimsrud, 1993gas phase; B
Quantity Value Units Method Reference Comment
Δr9.50kcal/molMoblGiles and Grimsrud, 1993gas phase; B

CHCl4- + 2Trichloromethane = C2H2Cl7-

By formula: CHCl4- + 2CHCl3 = C2H2Cl7-

Quantity Value Units Method Reference Comment
Δr14.70kcal/molN/AHiraoka, Mizuno, et al., 2001gas phase; B
Quantity Value Units Method Reference Comment
Δr7.25kcal/molTDAsHiraoka, Mizuno, et al., 2001gas phase; B

C2H2Cl7- + 3Trichloromethane = C3H3Cl10-

By formula: C2H2Cl7- + 3CHCl3 = C3H3Cl10-

Quantity Value Units Method Reference Comment
Δr11.80kcal/molN/AHiraoka, Mizuno, et al., 2001gas phase; B
Quantity Value Units Method Reference Comment
Δr5.24kcal/molTDAsHiraoka, Mizuno, et al., 2001gas phase; B

C4H9+ + Trichloromethane = (C4H9+ • Trichloromethane)

By formula: C4H9+ + CHCl3 = (C4H9+ • CHCl3)

Quantity Value Units Method Reference Comment
Δr9.1kcal/molPHPMSSharma, Meza de Hojer, et al., 1985gas phase; M
Quantity Value Units Method Reference Comment
Δr23.6cal/mol*KPHPMSSharma, Meza de Hojer, et al., 1985gas phase; M

Sodium hydroxide + Chloral = sodium formate + Trichloromethane

By formula: HNaO + C2HCl3O = CHNaO2 + CHCl3

Quantity Value Units Method Reference Comment
Δr-24.58kcal/molCmPritchard and Skinner, 1950liquid phase; Heat of hydrolysis; ALS

Trichloromethane + Chlorine = Carbon Tetrachloride + Hydrogen chloride

By formula: CHCl3 + Cl2 = CCl4 + HCl

Quantity Value Units Method Reference Comment
Δr-22.30kcal/molCmKirkbride, 1956liquid phase; Heat of chlorination; ALS

Iodide + Trichloromethane = (Iodide • Trichloromethane)

By formula: I- + CHCl3 = (I- • CHCl3)

Quantity Value Units Method Reference Comment
Δr14.1 ± 1.0kcal/molTDAsCaldwell, Masucci, et al., 1989gas phase; B,M

Trichloromethane + Bromine = Hydrogen bromide + Methane, bromotrichloro-

By formula: CHCl3 + Br2 = HBr + CBrCl3

Quantity Value Units Method Reference Comment
Δr-1.4 ± 0.1kcal/molEqkMendenhall, Golden, et al., 1973gas phase; ALS

2Fluorodichloromethane = Trichloromethane + Difluorochloromethane

By formula: 2CHCl2F = CHCl3 + CHClF2

Quantity Value Units Method Reference Comment
Δr-3.39 ± 0.48kcal/molEqkHess and Kemnitz, 1992gas phase; Gas Phase; ALS

C10H12Mo (cr) + 2Carbon Tetrachloride (l) = C10H10Cl2Mo (cr) + 2Trichloromethane (l)

By formula: C10H12Mo (cr) + 2CCl4 (l) = C10H10Cl2Mo (cr) + 2CHCl3 (l)

Quantity Value Units Method Reference Comment
Δr-76.8 ± 1.1kcal/molRSCCalado, Dias, et al., 1979MS

C10H12W (cr) + 2Carbon Tetrachloride (l) = C10H10Cl2W (cr) + 2Trichloromethane (l)

By formula: C10H12W (cr) + 2CCl4 (l) = C10H10Cl2W (cr) + 2CHCl3 (l)

Quantity Value Units Method Reference Comment
Δr-71.96 ± 0.81kcal/molRSCCalado, Dias, et al., 1979MS

Hydrogen bromide + Methane, bromotrichloro- = Trichloromethane + Bromine

By formula: HBr + CBrCl3 = CHCl3 + Br2

Quantity Value Units Method Reference Comment
Δr1.4kcal/molKinSullivan and Davidson, 1951gas phase; ALS

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
0.254500.LN/A 
0.274100.MN/A 
0.233800.MN/A 
0.25 MN/A 
0.263900.MN/A 
0.264000.XN/A 
0.24 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
0.497300.MN/A 
0.242200.XN/A 
0.235000.XN/A 
0.254100.XBarr and Newsham, 1987 
0.284600.MGossett, 1987 
0.264300.XN/A 
0.234200.XN/A 
0.254300.XN/A 
0.244200.MN/A 
0.33 MNicholson, Maguire, et al., 1984 
0.28 cNicholson, Maguire, et al., 1984 
0.32 CNicholson, Maguire, et al., 1984 
0.21 CNicholson, Maguire, et al., 1984 
0.203900.MN/ASolubility in sea water.
0.304400.XN/A 
0.254100.XLeighton and Calo, 1981 
0.27 LN/A 
0.155600.XN/A 
0.254600.XN/A 
0.25 VN/A 
0.90 VN/AValue at T = 275. K.
0.31 CN/A 
0.23 VN/A 
0.35 MPearson and McConnell, 1975The same data was also published in missing citation. Value at T = 293. K.
0.294800.MN/A 

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Notes

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

Chase, 1998
Chase, M.W., Jr., NIST-JANAF Themochemical Tables, Fourth Edition, J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]

Manion, 2002
Manion, J.A., Evaluated Enthalpies of Formation of the Stable Closed Shell C1 and C2 Chlorinated Hydrocarbons, J. Phys. Chem. Ref. Data, 2002, 31, 1, 123-172, https://doi.org/10.1063/1.1420703 . [all data]

Hu and Sinke, 1969
Hu, A.T.; Sinke, G.C., Combustion calorimetry of some chlorinated organic compounds, J. Chem. Thermodyn., 1969, 1, 6, 507, https://doi.org/10.1016/0021-9614(69)90010-X . [all data]

Hu and Sinke, 1969, 2
Hu, A.T.; Sinke, G.C., Combustion calorimetry of some chlorinated organic compounds, J. Chem. Thermodyn., 1969, 1, 507-513. [all data]

Smith, Bjellerup, et al., 1953
Smith, L.; Bjellerup, L.; Krook, S.; Westermark, H., Heats of combustion of organic chloro compounds determined by the "quartz wool" method, Acta Chem. Scand., 1953, 7, 65. [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]

Grolier, Roux-Desgranges, et al., 1993
Grolier, J.-P.E.; Roux-Desgranges, G.; Berkane, M.; Jimenez, E.; Wilhelm, E., Heat capacities and densities of mixtures of very polar substances 2. Mixtures containing N,N-dimethylformamide, J. Chem. Thermodynam., 1993, 25(1), 41-50. [all data]

Shehatta, 1993
Shehatta, I., Heat capacity at constant pressure of some halogen compounds, Thermochim. Acta, 1993, 213, 1-10. [all data]

Barta, Kooner, et al., 1989
Barta, L.; Kooner, Z.S.; Hepler, L.G.; Roux-Desgranges, G.; Grolier, J.-P.E., Thermodynamics of complex formation in chloroform and 1,4-dioxane, Can. J. Chem., 1989, 67, 1225-1229. [all data]

Barta, Kooner, et al., 1989, 2
Barta, L.; Kooner, Z.S.; Hepler, L.G.; Roux-Desgranges, G.; Grolier, J.-P.E., Thermal and volumetric properties of chloroform dimethylsulfoxide: Thermodynamic analysis using the ideal associated solution model, J. Solution Chem., 1989, 18(7), 663-673. [all data]

Petrov, Peshekhodov, et al., 1989
Petrov, A.N.; Peshekhodov, P.B.; Al'per, G.A., Heat capacity of non-aqueous solutions of non-electrolyts with N,N-dimethylformamide as a base, Sbornik Nauch. Trud., Termodin. Rast. neelect., Ivanovo, Inst. nevod. rast., 1989, Akad. [all data]

Grolier, Roux-Desgranges, et al., 1987
Grolier, J.-P.E.; Roux-Desgranges, G.; Kooner, Z.S.; Smith, J.F.; Hepler, L.G., Thermal and volumetric properties of chloroform + benzene mixtures and the ideal associated solution model of complex formation, J. Solution Chem., 1987, 16, 745-752. [all data]

Al'per, Peshekhodov, et al., 1986
Al'per, G.A.; Peshekhodov, P.B.; Nikiforov, M.Yu.; Petrov, A.N.; Krestov, G.A., Specific heats and features of the intermolecular interactions in the system chloroform-acetone, Zhur. Obshchei Khim., 1986, 56(8), 1688-1691. [all data]

Hepler, Kooner, et al., 1985
Hepler, L.G.; Kooner, Z.S.; Roux-Desgranges, G.; Grolier, J.-P.E., Thermal and volumetric properties of chloroform + triethylamine mixtures and the ideal associated solution model of complex formation, J. Solution Chem., 1985, 14(8), 579-594. [all data]

Inglese, Castagnolo, et al., 1981
Inglese, A.; Castagnolo, M.; Dell'Atti, A.; DeGiglio, A., Thermochim. Acta, 1981, 77-87. [all data]

Rastorguev and Ganiev, 1967
Rastorguev, Yu.L.; Ganiev, Yu.A., Study of the heat capacity of selected solvents, Izv. Vyssh. Uchebn. Zaved. Neft Gaz. 10, 1967, No.1, 79-82. [all data]

Harrison and Moelwyn-Hughes, 1957
Harrison, D.; Moelwyn-Hughes, E.A., The heat capacities of certain liquids, Proc. Roy. Soc. (London), 1957, A239, 230-246. [all data]

Staveley, Tupman, et al., 1955
Staveley, L.A.K.; Tupman, W.I.; Hart, K.R., Some thermodynamice properties of the systems benzene + ethylene dichloride, benzene + carbon tetrachloride, acetone + chloroform, and acetone + carbon disulphide, Trans. Faraday Soc., 1955, 51, 323-342. [all data]

Kurbatov, 1948
Kurbatov, V.Ya., Heat capacity of liquids. 2. Heat capacity and the temperature dependence of heat capacity from halogen derivatives of acylic hydrocarbons, Zh. Obshch. Kim., 1948, 18, 372-389. [all data]

Phillip, 1939
Phillip, N.M., Adiabatic and isothermal compressibilities of liquids, Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]

Richards and Wallace, 1932
Richards, W.T.; Wallace, J.H., Jr., The specific heats of five organic liquids from their adiabatic temperature-pressure coefficients, J. Am. Chem. Soc., 1932, 54, 2705-2713. [all data]

Williams and Daniels, 1925
Williams, J.W.; Daniels, F., The specific heats of binary mixtures, J. Am. Chem. Soc., 1925, 47, 1490-1503. [all data]

Willams and Daniels, 1924
Willams, J.W.; Daniels, F., The specific heats of certain organic liquids at elevated temperatures, J. Am. Chem. Soc., 1924, 46, 903-917. [all data]

Stull, 1937
Stull, D.R., A Semi-micro Calorimeter for Measuring Heat Capacities at Low Temp., J. Am. Chem. Soc., 1937, 59, 2726. [all data]

Campbell and Chatterjee, 1969
Campbell, A.N.; Chatterjee, R.M., The critical constants and orthobaric densities of acetone, chloroform benzene, and carbon tetrachloride, Can. J. Chem., 1969, 47, 3893-8. [all data]

Campbell and Chatterjee, 1968
Campbell, A.N.; Chatterjee, R.M., Orthobaric Data of Certain Pure Liquids in the Neighborhood of the Critical Point, Can. J. Chem., 1968, 46, 575-81. [all data]

Herz and Neukirch, 1923
Herz, W.; Neukirch, E., On Knowldge of the Critical State, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1923, 104, 433-50. [all data]

Majer and Svoboda, 1985
Majer, V.; Svoboda, V., Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]

Majer, Sváb, et al., 1980
Majer, V.; Sváb, L.; Svoboda, V., Enthalpies of vaporization and cohesive energies for a group of chlorinated hydrocarbons, The Journal of Chemical Thermodynamics, 1980, 12, 9, 843-847, https://doi.org/10.1016/0021-9614(80)90028-2 . [all data]

Mathews, 1926
Mathews, J.H., The accurate measurement of heats of vaporization of liquids, J. Am. Chem. Soc., 1926, 48, 562-576. [all data]

Pedley, Naylor, et al., 1986
Pedley, J.B.; Naylor, R.D.; Kirby, S.P., Thermochemical Data of Organic Compounds, Chapman and Hall, New York, 1986, 1-792. [all data]

Chen, Wang, et al., 1995
Chen, Geng-Hua; Wang, Qi; Ma, Zhong-Min; Yan, Xin-Huan; Han, Shi-Jun, Phase equilibria at superatmospheric pressures for systems containing halohydrocarbon, aromatic hydrocarbon, and alcohol, J. Chem. Eng. Data, 1995, 40, 2, 361-366, https://doi.org/10.1021/je00018a003 . [all data]

Stephenson and Malanowski, 1987
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Notes

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