1-Butanol
- Formula: C4H10O
- Molecular weight: 74.1216
- IUPAC Standard InChIKey: LRHPLDYGYMQRHN-UHFFFAOYSA-N
- CAS Registry Number: 71-36-3
- 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. - Other names: Butyl alcohol; n-Butan-1-ol; n-Butanol; n-Butyl alcohol; Butyl hydroxide; CCS 203; Hemostyp; Methylolpropane; Propylcarbinol; n-C4H9OH; Butanol; Butan-1-ol; 1-Hydroxybutane; Alcool butylique; Butanolo; Butylowy alkohol; Butyric alcohol; Propylmethanol; Butanolen; 1-Butyl alcohol; Rcra waste number U031; Butanol-1; NSC 62782
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -66. ± 1. | kcal/mol | AVG | N/A | Average of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 86.515 | cal/mol*K | N/A | Chao J., 1986 | Other values of S(298.15 K) based on low-temperature thermal measurements are (in J/mol*K): 363.17 [65COU/HAL], 362.33 [ Chermin H.A.G., 1961], and 361.9 [ Buckley E., 1967].; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
10.17 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Recommended S(T) and Cp(T) values agree with those calculated by [ Chermin H.A.G., 1961] within 1.5 J/mol*K. S(T) values calculated by [ Dyatkina M.E., 1954] are different from values given here by 12-30 J/mol*K. Please also see Chao J., 1986.; GT |
13.94 | 100. | ||
16.75 | 150. | ||
19.43 | 200. | ||
24.063 | 273.15 | ||
25.820 ± 0.060 | 298.15 | ||
25.951 | 300. | ||
33.021 | 400. | ||
39.297 | 500. | ||
44.546 | 600. | ||
48.956 | 700. | ||
52.715 | 800. | ||
55.963 | 900. | ||
58.779 | 1000. | ||
61.228 | 1100. | ||
63.360 | 1200. | ||
65.215 | 1300. | ||
66.833 | 1400. | ||
68.246 | 1500. | ||
71.06 | 1750. | ||
73.09 | 2000. | ||
74.62 | 2250. | ||
75.74 | 2500. | ||
76.60 | 2750. | ||
77.25 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.68 ± 0.19 | 395.25 | Stromsoe E., 1970 | Ideal gas heat capacities are given by [ Stromsoe E., 1970] as a linear function Cp=f1*(a+bT). This expression approximates the experimental values with the average deviation of 0.79 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%.; GT |
32.954 | 398.15 | ||
34.18 ± 0.19 | 404.15 | ||
34.46 ± 0.19 | 409.15 | ||
33.953 | 413.15 | ||
35.03 ± 0.19 | 419.55 | ||
35.67 ± 0.19 | 431.05 | ||
35.234 | 433.15 | ||
36.23 ± 0.19 | 441.15 | ||
36.487 | 453.15 | ||
37.26 ± 0.19 | 459.55 | ||
38.85 ± 0.19 | 488.25 | ||
40.62 ± 0.19 | 520.05 | ||
42.06 ± 0.19 | 545.95 | ||
43.31 ± 0.19 | 568.45 | ||
45.25 ± 0.19 | 603.35 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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:
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 | -79. ± 1. | kcal/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -638. ± 5. | kcal/mol | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 53.951 | cal/mol*K | N/A | Counsell, Hales, et al., 1965 | DH |
S°liquid | 54.49 | cal/mol*K | N/A | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 46.02 J/mol*K. Revision of previous data.; DH |
S°liquid | 60.21 | cal/mol*K | N/A | Parks, 1925 | Extrapolation below 90 K, 73.81 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
42.271 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
42.225 | 298.15 | Gates, Wood, et al., 1986 | T = 298.15 to 368.15 K.; DH |
42.47 | 298. | Korolev, Kukharenko, et al., 1986 | DH |
45.94 | 321.05 | Naziev, Bashirov, et al., 1986 | T = 321.05, 349.20, 373.35 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.5934 kJ/kg*K.; DH |
42.347 | 298.15 | Ogawa and Murakami, 1986 | DH |
42.058 | 298.15 | Roux-Dexgranges, Grolier, et al., 1986 | DH |
42.230 | 298.15 | Tanaka, Toyama, et al., 1986 | DH |
42.323 | 298.15 | Zegers and Somsen, 1984 | DH |
41.66 | 293.15 | Arutyunyan, Bagdasaryan, et al., 1981 | T = 293 to 373 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.351 kJ/kg*K. Cp given from 293.15 to 533.15 for pressure range 10 to 60 MPa.; DH |
43.40 | 303.5 | Griigo'ev, Yanin, et al., 1979 | T = 303 to 462 K. p = 0.98 bar.; DH |
42.90 | 301.2 | Paz Andrade, Paz, et al., 1970 | T = 28, 40°C.; DH |
42.311 | 298.15 | Counsell, Hales, et al., 1965 | T = 11 to 323 K.; DH |
45.20 | 323. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 21 to 78°C.; DH |
51.51 | 302.6 | Phillip, 1939 | DH |
43.81 | 298. | Trew and Watkins, 1933 | DH |
41.90 | 294.0 | Parks, 1925 | T = 90 to 294 K. Value is unsmoothed experimental datum.; DH |
43.09 | 303. | Willams and Daniels, 1924 | T = 303 to 343 K. Equation only.; DH |
41.71 | 298. | von Reis, 1881 | T = 290 to 390 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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 390.6 ± 0.8 | K | AVG | N/A | Average of 137 out of 146 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 188. ± 9. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 184.54 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 184.51 | K | N/A | Counsell, Hales, et al., 1965, 2 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 183.9 | K | N/A | Parks, 1925, 2 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 562. ± 2. | K | AVG | N/A | Average of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 45. ± 4. | atm | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.274 | l/mol | N/A | Gude and Teja, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.65 ± 0.06 | mol/l | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 12.4 ± 0.6 | kcal/mol | AVG | N/A | Average of 15 out of 16 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
10.35 | 390.9 | N/A | Majer and Svoboda, 1985 | |
11.0 | 372. | EB | Muñoz and Krähenbühl, 2001 | Based on data from 357. to 389. K.; AC |
9.13 | 423. | N/A | Wormald and Fennell, 2000 | AC |
7.07 | 473. | N/A | Wormald and Fennell, 2000 | AC |
4.97 | 523. | N/A | Wormald and Fennell, 2000 | AC |
11.9 | 330. | N/A | Dejoz, Cruz Burguet, et al., 1995 | Based on data from 315. to 390. K.; AC |
10.8 | 379. | N/A | Susial and Ortega, 1993 | Based on data from 364. to 403. K.; AC |
10.8 | 387. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 399. K.; AC |
12.0 | 338. | A | Stephenson and Malanowski, 1987 | Based on data from 323. to 413. K.; AC |
10.0 | 428. | A | Stephenson and Malanowski, 1987 | Based on data from 413. to 550. K.; AC |
12.3 | 236. | A | Stephenson and Malanowski, 1987 | Based on data from 209. to 251. K.; AC |
10.9 | 386. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 397. K.; AC |
10.5 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 429. K.; AC |
10.0 | 430. | A | Stephenson and Malanowski, 1987 | Based on data from 415. to 501. K.; AC |
8.94 | 512. | A | Stephenson and Malanowski, 1987 | Based on data from 497. to 563. K.; AC |
11.3 | 366. | EB | Stephenson and Malanowski, 1987 | Based on data from 351. to 397. K. See also Ambrose, Counsell, et al., 1970.; AC |
11.7 | 344. | N/A | Sachek, Peshchenko, et al., 1982 | Based on data from 329. to 391. K.; AC |
11.8 ± 0.02 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
11.6 ± 0.02 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
11.4 ± 0.02 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
11.1 ± 0.02 | 363. | C | Svoboda, Veselý, et al., 1973 | AC |
13.1 | 303. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 288. to 404. K.; AC |
12.7 | 310. | DTA | Kemme and Kreps, 1969 | Based on data from 295. to 391. K.; AC |
11.3 ± 0.02 | 356. | C | Counsell, Hales, et al., 1965, 2 | AC |
10.9 ± 0.02 | 381. | C | Counsell, Hales, et al., 1965, 2 | AC |
10.3 ± 0.02 | 391. | C | Counsell, Hales, et al., 1965, 2 | AC |
10.1 | 434. | N/A | Ambrose and Townsend, 1963 | Based on data from 419. to 563. K.; AC |
11.1 | 377. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 362. to 398. K.; AC |
11.5 | 352. | N/A | Brown and Smith, 1959 | Based on data from 337. to 390. K. See also Boublik, Fried, et al., 1984.; AC |
11.5 | 352. | N/A | Kahlbaum, 1898 | Based on data from 314. to 390. K. See also Boublik, Fried, et al., 1984.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 298. to 410. |
---|---|
A (kcal/mol) | 14.95 |
α | -0.6584 |
β | 0.696 |
Tc (K) | 562.9 |
Reference | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
295.8 to 391.0 | 4.54036 | 1351.555 | -93.34 | Kemme and Kreps, 1969 | |
391. to 479. | 4.38460 | 1254.502 | -105.246 | Hessel and Geiseler, 1965 | Coefficents calculated by NIST from author's data. |
419.34 to 562.98 | 4.42350 | 1305.001 | -94.676 | Ambrose and Townsend, 1963, 2 | Coefficents calculated by NIST from author's data. |
362.36 to 398.84 | 4.49822 | 1313.878 | -98.789 | Biddiscombe, Collerson, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.240 | 184.5 | Counsell, Hales, et al., 1965 | DH |
2.22 | 183.9 | Acree, 1991 | AC |
2.218 | 183.9 | Parks, 1925 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
12.14 | 184.5 | Counsell, Hales, et al., 1965 | DH |
12.06 | 183.9 | Parks, 1925 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Gas phase ion energetics 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 |
---|---|---|---|---|
130. | 7200. | M | N/A | |
120. | C | N/A | ||
53. | M | N/A | Value at T = 303. K. | |
110. | M | Buttery, Ling, et al., 1969 | ||
140. | M | N/A | ||
120. | M | Butler, Ramchandani, et al., 1935 | This paper supersedes earlier work with more concentrated solutions Butler, Thomson, et al., 1933. |
Gas phase ion energetics 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
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) | 9.99 ± 0.05 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 188.6 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 181.4 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.10 ± 0.05 | EI | Holmes and Lossing, 1991 | LL |
9.99 ± 0.05 | PIPECO | Shao, Baer, et al., 1988 | LL |
10.64 ± 0.07 | EI | Bowen and Maccoll, 1984 | LBLHLM |
10.09 ± 0.02 | PE | Cocksey, Eland, et al., 1971 | LLK |
10.37 | PE | Baker, Betteridge, et al., 1971 | LLK |
10.37 | PE | Baker, Betteridge, et al., 1971 | LLK |
10.04 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
10.43 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
10.44 ± 0.03 | PE | Peel and Willett, 1975 | Vertical value; LLK |
10.37 | PE | Katsumata, Iwai, et al., 1973 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH3O+ | 11.36 ± 0.06 | n-C3H7 | EI | Selim and Helal, 1981 | LLK |
CH3O+ | 11.46 | ? | EI | Lambdin, Tuffly, et al., 1959 | RDSH |
C2H2O+ | 11.23 | ? | EI | Lambdin, Tuffly, et al., 1959 | RDSH |
C4H8+ | 10.18 ± 0.05 | H2O | PIPECO | Shao, Baer, et al., 1988 | LL |
C4H8+ | 10.20 ± 0.10 | H2O | EI | Bowen and Maccoll, 1984 | LBLHLM |
De-protonation reactions
C4H9O- + =
By formula: C4H9O- + H+ = C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 375.3 ± 2.0 | kcal/mol | CIDC | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
ΔrH° | 375.4 ± 2.1 | kcal/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 375.0 ± 2.9 | kcal/mol | G+TS | Boand, Houriet, et al., 1983 | gas phase; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 368.7 ± 2.1 | kcal/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
ΔrG° | 368.8 ± 2.0 | kcal/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 368.4 ± 2.8 | kcal/mol | CIDC | Boand, Houriet, et al., 1983 | gas phase; value altered from reference due to change in acidity scale; B |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Chao J., 1986
Chao J.,
Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties,
J. Phys. Chem. Ref. Data, 1986, 15, 1369-1436. [all data]
Chermin H.A.G., 1961
Chermin H.A.G.,
Thermo data for petrochemicals. Part 28. Gaseous normal alcohols. The important thermo properties are presented for all the gaseous normal alcohols from methanol through n-decanol,
Petrol. Refiner, 1961, 40 (4), 127-130. [all data]
Buckley E., 1967
Buckley E.,
Chemical equilibria. Part 2. Dehydrogenation of propanol and butanol,
Trans. Faraday Soc., 1967, 63, 895-901. [all data]
Thermodynamics Research Center, 1997
Thermodynamics Research Center,
Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
Dyatkina M.E., 1954
Dyatkina M.E.,
Thermodynamic functions of normal alcohols (propanol, butanol, ethylene glycol),
Zh. Fiz. Khim., 1954, 28, 377. [all data]
Stromsoe E., 1970
Stromsoe E.,
Heat capacity of alcohol vapors at atmospheric pressure,
J. Chem. Eng. Data, 1970, 15, 286-290. [all data]
Counsell, Hales, et al., 1965
Counsell, J.F.; Hales, J.L.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part 16. Butyl alcohol,
Trans. Faraday Soc., 1965, 61, 1869-1875. [all data]
Parks, Kelley, et al., 1929
Parks, G.S.; Kelley, K.K.; Huffman, H.M.,
Thermal data on organic compounds. V. A revision of the entropies and free energies of nineteen organic compounds,
J. Am. Chem. Soc., 1929, 51, 1969-1973. [all data]
Parks, 1925
Parks, G.S.,
Thermal data on organic compounds I. The heat capacities and free energies of methyl, ethyl and normal-butyl alcohols,
J. Am. Chem. Soc., 1925, 47, 338-345. [all data]
Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M.,
Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc.,
Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]
Gates, Wood, et al., 1986
Gates, J.A.; Wood, R.H.; Cobos, J.C.; Casanova, C.; Roux, A.H.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Densities and heat capacities of 1-butanol + n-decane from 298 K to 400 K,
Fluid Phase Equilib., 1986, 27, 137-151. [all data]
Korolev, Kukharenko, et al., 1986
Korolev, V.P.; Kukharenko, V.A.; Krestov, G.A.,
Specific heat of binary mixtures of aliphatic alcohols with N,N-dimethylformamide and dimethylsulphoxide,
Zhur. Fiz. Khim., 1986, 60, 1854-1857. [all data]
Naziev, Bashirov, et al., 1986
Naziev, Ya.M.; Bashirov, M.M.; Badalov, Yu.A.,
Experimental device for measurement of isobaric specific heat of electrolytes at elevated pressures,
Inzh-Fiz. Zhur., 1986, 51(5), 789-795. [all data]
Ogawa and Murakami, 1986
Ogawa, H.; Murakami, S.,
Excess isobaric heat capacities for water + alkanol mixtures at 298.15 K,
Thermochim. Acta, 1986, 109, 145-154. [all data]
Roux-Dexgranges, Grolier, et al., 1986
Roux-Dexgranges, G.; Grolier, J.-P.E.; Villamanan, M.A.; Casanova, C.,
Role of alcohol in microemulsions. III. Volumes and heat capacities in the continuious phase water-n-butanol-toluene of reverse micelles,
Fluid Phase Equilibria, 1986, 25, 209-230. [all data]
Tanaka, Toyama, et al., 1986
Tanaka, R.; Toyama, S.; Murakami, S.,
Heat capacities of {xCnH2n+1OH+(1-x)C7H16} for n = 1 to 6 at 298.15 K,
J. Chem. Thermodynam., 1986, 18, 63-73. [all data]
Zegers and Somsen, 1984
Zegers, H.C.; Somsen, G.,
Partial molar volumes and heat capacities in (dimethylformamide + an n-alkanol),
J. Chem. Thermodynam., 1984, 16, 225-235. [all data]
Arutyunyan, Bagdasaryan, et al., 1981
Arutyunyan, G.S.; Bagdasaryan, S.S.; Kerimov, A.M.,
Experimental investigation of the isobaric heat capacity of n-propyl, n-butyl and n-amyl alcohols at different temperatures and pressures,
Izv. Akad. Nauk Azerb. SSr, 1981, (6), 94-97. [all data]
Griigo'ev, Yanin, et al., 1979
Griigo'ev, B.A.; Yanin, G.S.; Rastorguev, Yu.L.; Thermophysical parameters of alcohols, Tr. GIAP,
54, 1979, 57-64. [all data]
Paz Andrade, Paz, et al., 1970
Paz Andrade, M.I.; Paz, J.M.; Recacho, E.,
Contribucion a la microcalorimetria de los calores especificos de solidos y liquidos,
An. Quim., 1970, 66, 961-967. [all data]
Swietoslawski and Zielenkiewicz, 1960
Swietoslawski, W.; Zielenkiewicz, A.,
Mean specific heat in homologous series of binary and ternary positive azeotropes,
Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1960, 8, 651-653. [all data]
Phillip, 1939
Phillip, N.M.,
Adiabatic and isothermal compressibilities of liquids,
Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]
Trew and Watkins, 1933
Trew, V.C.G.; Watkins, G.M.C.,
Some physical properties of mixtures of certain organic liquids,
Trans. Faraday Soc., 1933, 29, 1310-1318. [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]
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume 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 ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy 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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