Trichloromethane
- Formula: CHCl3
- Molecular weight: 119.378
- IUPAC Standard InChIKey: HEDRZPFGACZZDS-UHFFFAOYSA-N
- CAS Registry Number: 67-66-3
- 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. - Isotopologues:
- Other names: Chloroform; Freon 20; Methane, trichloro-; R 20; Trichloroform; CHCl3; Formyl trichloride; Methane trichloride; Methenyl trichloride; Methyl trichloride; Chloroforme; Cloroformio; NCI-C02686; R 20 (refrigerant); Trichloormethaan; Trichlormethan; Triclorometano; Rcra waste number U044; UN 1888; NSC 77361; F 20
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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 |
---|---|---|---|---|---|
ΔfH°gas | -24.661 | kcal/mol | Review | Chase, 1998 | Data last reviewed in December, 1968 |
ΔfH°gas | -24.59 ± 0.60 | kcal/mol | Review | Manion, 2002 | derived from recommended ΔfHliquid° and ΔvapH°; DRB |
Quantity | Value | Units | Method | Reference | Comment |
S°gas,1 bar | 70.652 | cal/mol*K | Review | Chase, 1998 | Data 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 | 10.57530 | 24.25339 |
B | 27.40760 | 0.819731 |
C | -21.22810 | -0.157110 |
D | 6.190230 | 0.010446 |
E | -0.124954 | -2.234230 |
F | -29.27560 | -37.23709 |
G | 75.46489 | 92.53241 |
H | -24.65990 | -24.65990 |
Reference | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in December, 1968 | Data last reviewed in December, 1968 |
Condensed phase thermochemistry data
Go To: Top, Gas 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.
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 | -32.05 ± 0.60 | kcal/mol | Review | Manion, 2002 | adopted combustion calorimetry data of Hu and Sinke, 1969 with increased uncertainty to reflect other data; DRB |
ΔfH°liquid | -32.10 | kcal/mol | Ccr | Hu and Sinke, 1969, 2 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -113.10 | kcal/mol | Ccr | Hu and Sinke, 1969, 2 | ALS |
ΔcH°liquid | -113.3 ± 2.0 | kcal/mol | Ccb | Smith, Bjellerup, et al., 1953 | Reanalyzed 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 |
---|---|---|---|
27.306 | 298.15 | Grolier, Roux-Desgranges, et al., 1993 | DH |
27.06 | 298.15 | Shehatta, 1993 | DH |
27.323 | 298.15 | Barta, Kooner, et al., 1989 | DH |
27.330 | 298.15 | Barta, Kooner, et al., 1989, 2 | DH |
27.61 | 298.15 | Petrov, Peshekhodov, et al., 1989 | T = 258.15, 278.15, 298.15, 318.15 K.; DH |
27.211 | 298.15 | Grolier, Roux-Desgranges, et al., 1987 | DH |
27.61 | 298.15 | Al'per, Peshekhodov, et al., 1986 | DH |
27.182 | 298.15 | Hepler, Kooner, et al., 1985 | DH |
27.309 | 298.15 | Inglese, Castagnolo, et al., 1981 | DH |
27.77 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 333 K.; DH |
27.10 | 300. | Harrison and Moelwyn-Hughes, 1957 | T = 243 to 303 K.; DH |
27.25 | 303.2 | Harrison and Moelwyn-Hughes, 1957 | T = 245 to 303 K. Unsmoothed experimental datum.; DH |
27.290 | 298. | Staveley, Tupman, et al., 1955 | T = 284 to 329 K.; DH |
27.99 | 298. | Kurbatov, 1948 | T = -52 to 51°C. Mean Cp, four temperatures.; DH |
33.39 | 303.6 | Phillip, 1939 | DH |
27.01 | 298.1 | Richards and Wallace, 1932 | T = 293 to 323 K.; DH |
27.61 | 293.2 | Williams and Daniels, 1925 | T = 20 to 50°C.; DH |
27.89 | 303. | Willams and Daniels, 1924 | T = 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 |
---|---|---|---|---|---|
Tboil | 334.3 ± 0.2 | K | AVG | N/A | Average of 36 out of 37 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 210. ± 2. | K | AVG | N/A | Average of 14 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 209.61 | K | N/A | Stull, 1937 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 537. ± 2. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 52.5900 | atm | N/A | Campbell and Chatterjee, 1969 | Uncertainty assigned by TRC = 0.09998 atm; TRC |
Pc | 52.5900 | atm | N/A | Campbell and Chatterjee, 1968 | Uncertainty assigned by TRC = 0.0599 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.11 | mol/l | N/A | Campbell and Chatterjee, 1969 | Uncertainty assigned by TRC = 0.03 mol/l; TRC |
ρc | 3.84 | mol/l | N/A | Campbell and Chatterjee, 1968 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 4.15 | mol/l | N/A | Herz and Neukirch, 1923 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 7.50 | kcal/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 7.49 ± 0.02 | kcal/mol | Review | Manion, 2002 | weighted average of several measurements plus a correction for non-ideality; DRB |
ΔvapH° | 7.43 | kcal/mol | C | Majer, Sváb, et al., 1980 | AC |
ΔvapH° | 7.30 ± 0.10 | kcal/mol | V | Mathews, 1926 | Reanalyzed 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 |
---|---|---|---|---|
6.989 | 334.3 | N/A | Majer and Svoboda, 1985 | |
7.36 | 321. | N/A | Chen, Wang, et al., 1995 | Based on data from 306. to 427. K.; AC |
7.60 | 254. | A | Stephenson and Malanowski, 1987 | Based on data from 227. to 269. K.; AC |
7.27 | 348. | A | Stephenson and Malanowski, 1987 | Based on data from 333. to 416. K.; AC |
6.91 | 425. | A | Stephenson and Malanowski, 1987 | Based on data from 410. to 481. K.; AC |
7.19 | 494. | A | Stephenson and Malanowski, 1987 | Based on data from 479. to 523. K.; AC |
7.77 | 275. | EB | Boublík and Aim, 1972 | Based on data from 260. to 333. K.; AC |
8.37 | 230. | N/A | Stull, 1947 | Based on data from 215. to 334. K.; AC |
7.39 | 320. | N/A | Scatchard and Raymond, 1938 | Based 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 334.4 | 4.20201 | 1233.129 | -40.953 | Stull, 1947 | Coefficents calculated by NIST from author's data. |
334.4 to 527. | 4.56421 | 1486.455 | -8.612 | Stull, 1947 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.1 | 209.6 | Acree, 1991 | AC |
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
By formula: Cl- + CHCl3 = (Cl- • CHCl3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.2 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; B,M |
ΔrH° | 19.5 ± 2.0 | kcal/mol | TDAs | Hiraoka, Mizuno, et al., 2001 | gas phase; B |
ΔrH° | 18.10 | kcal/mol | Mobl | Giles and Grimsrud, 1993 | gas phase; B |
ΔrH° | 18.1 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrH° | 19.10 ± 0.70 | kcal/mol | TDEq | Dougherty, Dalton, et al., 1974 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 23.2 | cal/mol*K | N/A | Larson and McMahon, 1984 | gas phase; From thermochemical cycle(Cl-)CF3H, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
ΔrS° | 24.5 | cal/mol*K | HPMS | Dougherty, Dalton, et al., 1974 | gas phase; M |
ΔrS° | 14.8 | cal/mol*K | PHPMS | Yamdagni and Kebarle, 1971 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 11. ± 1. | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
CCl3- + =
By formula: CCl3- + H+ = CHCl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 360.33 | kcal/mol | Acid | Paulino and Squires, 1991 | gas phase; B |
ΔrH° | 357.6 ± 2.1 | kcal/mol | G+TS | Paulino and Squires, 1991 | gas phase; B |
ΔrH° | 357.0 ± 6.1 | kcal/mol | G+TS | Bohme, Lee-Ruff, et al., 1972 | gas phase; > acetone, <= C5H6; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 349.9 ± 2.0 | kcal/mol | IMRB | Paulino and Squires, 1991 | gas phase; B |
ΔrG° | 349.9 ± 3.0 | kcal/mol | IMRB | Born, Ingemann, et al., 2000 | gas phase; B |
ΔrG° | 349.3 ± 6.0 | kcal/mol | IMRB | Bohme, Lee-Ruff, et al., 1972 | gas phase; > acetone, <= C5H6; value altered from reference due to change in acidity scale; B |
By formula: CN- + CHCl3 = (CN- • CHCl3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.2 ± 3.5 | kcal/mol | IMRE | Larson and McMahon, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.8 | cal/mol*K | N/A | Larson and McMahon, 1987 | gas phase; switching reaction,Thermochemical ladder(CN-)H2O, Entropy change calculated or estimated; Payzant, Yamdagni, et al., 1971; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 10.8 ± 2.3 | kcal/mol | IMRE | Larson and McMahon, 1987 | gas phase; B,M |
C8H6MoO3 (solution) + (solution) = (solution) + (solution)
By formula: C8H6MoO3 (solution) + CCl4 (solution) = C8H5ClMoO3 (solution) + CHCl3 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -31.81 ± 0.91 | kcal/mol | RSC | Nolan, López de la Vega, et al., 1986 | solvent: 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 |
By formula: Br- + CHCl3 = (Br- • CHCl3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.80 | kcal/mol | Mobl | Giles and Grimsrud, 1993 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 9.50 | kcal/mol | Mobl | Giles and Grimsrud, 1993 | gas phase; B |
By formula: CHCl4- + 2CHCl3 = C2H2Cl7-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.70 | kcal/mol | N/A | Hiraoka, Mizuno, et al., 2001 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 7.25 | kcal/mol | TDAs | Hiraoka, Mizuno, et al., 2001 | gas phase; B |
By formula: C2H2Cl7- + 3CHCl3 = C3H3Cl10-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.80 | kcal/mol | N/A | Hiraoka, Mizuno, et al., 2001 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 5.24 | kcal/mol | TDAs | Hiraoka, Mizuno, et al., 2001 | gas phase; B |
By formula: C4H9+ + CHCl3 = (C4H9+ • CHCl3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.1 | kcal/mol | PHPMS | Sharma, Meza de Hojer, et al., 1985 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 23.6 | cal/mol*K | PHPMS | Sharma, Meza de Hojer, et al., 1985 | gas phase; M |
By formula: HNaO + C2HCl3O = CHNaO2 + CHCl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -24.58 | kcal/mol | Cm | Pritchard and Skinner, 1950 | liquid phase; Heat of hydrolysis; ALS |
By formula: CHCl3 + Cl2 = CCl4 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -22.30 | kcal/mol | Cm | Kirkbride, 1956 | liquid phase; Heat of chlorination; ALS |
By formula: I- + CHCl3 = (I- • CHCl3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.1 ± 1.0 | kcal/mol | TDAs | Caldwell, Masucci, et al., 1989 | gas phase; B,M |
By formula: CHCl3 + Br2 = HBr + CBrCl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.4 ± 0.1 | kcal/mol | Eqk | Mendenhall, Golden, et al., 1973 | gas phase; ALS |
By formula: 2CHCl2F = CHCl3 + CHClF2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.39 ± 0.48 | kcal/mol | Eqk | Hess and Kemnitz, 1992 | gas phase; Gas Phase; ALS |
C10H12Mo (cr) + 2 (l) = C10H10Cl2Mo (cr) + 2 (l)
By formula: C10H12Mo (cr) + 2CCl4 (l) = C10H10Cl2Mo (cr) + 2CHCl3 (l)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -76.8 ± 1.1 | kcal/mol | RSC | Calado, Dias, et al., 1979 | MS |
C10H12W (cr) + 2 (l) = C10H10Cl2W (cr) + 2 (l)
By formula: C10H12W (cr) + 2CCl4 (l) = C10H10Cl2W (cr) + 2CHCl3 (l)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -71.96 ± 0.81 | kcal/mol | RSC | Calado, Dias, et al., 1979 | MS |
By formula: HBr + CBrCl3 = CHCl3 + Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.4 | kcal/mol | Kin | Sullivan and Davidson, 1951 | gas phase; ALS |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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 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 |
---|---|---|---|---|
0.25 | 4500. | L | N/A | |
0.27 | 4100. | M | N/A | |
0.23 | 3800. | M | N/A | |
0.25 | M | N/A | ||
0.26 | 3900. | M | N/A | |
0.26 | 4000. | X | N/A | |
0.24 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.49 | 7300. | M | N/A | |
0.24 | 2200. | X | N/A | |
0.23 | 5000. | X | N/A | |
0.25 | 4100. | X | Barr and Newsham, 1987 | |
0.28 | 4600. | M | Gossett, 1987 | |
0.26 | 4300. | X | N/A | |
0.23 | 4200. | X | N/A | |
0.25 | 4300. | X | N/A | |
0.24 | 4200. | M | N/A | |
0.33 | M | Nicholson, Maguire, et al., 1984 | ||
0.28 | c | Nicholson, Maguire, et al., 1984 | ||
0.32 | C | Nicholson, Maguire, et al., 1984 | ||
0.21 | C | Nicholson, Maguire, et al., 1984 | ||
0.20 | 3900. | M | N/A | Solubility in sea water. |
0.30 | 4400. | X | N/A | |
0.25 | 4100. | X | Leighton and Calo, 1981 | |
0.27 | L | N/A | ||
0.15 | 5600. | X | N/A | |
0.25 | 4600. | X | N/A | |
0.25 | V | N/A | ||
0.90 | V | N/A | Value at T = 275. K. | |
0.31 | C | N/A | ||
0.23 | V | N/A | ||
0.35 | M | Pearson and McConnell, 1975 | The same data was also published in missing citation. Value at T = 293. K. | |
0.29 | 4800. | M | N/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]
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°gas,1 bar Entropy of gas at standard conditions (1 bar) Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction 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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