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, 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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -277. ± 5. | kJ/mol | AVG | N/A | Average of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 361.98 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
42.54 | 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 |
58.33 | 100. | ||
70.10 | 150. | ||
81.28 | 200. | ||
100.68 | 273.15 | ||
108.03 ± 0.25 | 298.15 | ||
108.58 | 300. | ||
138.16 | 400. | ||
164.42 | 500. | ||
186.38 | 600. | ||
204.83 | 700. | ||
220.56 | 800. | ||
234.15 | 900. | ||
245.93 | 1000. | ||
256.18 | 1100. | ||
265.10 | 1200. | ||
272.86 | 1300. | ||
279.63 | 1400. | ||
285.54 | 1500. | ||
297.3 | 1750. | ||
305.8 | 2000. | ||
312.2 | 2250. | ||
316.9 | 2500. | ||
320.5 | 2750. | ||
323.2 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
140.93 ± 0.79 | 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 |
137.88 | 398.15 | ||
143.00 ± 0.79 | 404.15 | ||
144.16 ± 0.79 | 409.15 | ||
142.06 | 413.15 | ||
146.58 ± 0.79 | 419.55 | ||
149.26 ± 0.79 | 431.05 | ||
147.42 | 433.15 | ||
151.60 ± 0.79 | 441.15 | ||
152.66 | 453.15 | ||
155.88 ± 0.79 | 459.55 | ||
162.55 ± 0.79 | 488.25 | ||
169.95 ± 0.79 | 520.05 | ||
175.97 ± 0.79 | 545.95 | ||
181.20 ± 0.79 | 568.45 | ||
189.31 ± 0.79 | 603.35 |
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:
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 | -328. ± 4. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2670. ± 20. | kJ/mol | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 225.73 | J/mol*K | N/A | Counsell, Hales, et al., 1965 | DH |
S°liquid | 228.0 | J/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 | 251.9 | J/mol*K | N/A | Parks, 1925 | Extrapolation below 90 K, 73.81 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
176.86 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
176.67 | 298.15 | Gates, Wood, et al., 1986 | T = 298.15 to 368.15 K.; DH |
177.7 | 298. | Korolev, Kukharenko, et al., 1986 | DH |
192.2 | 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 |
177.18 | 298.15 | Ogawa and Murakami, 1986 | DH |
175.97 | 298.15 | Roux-Dexgranges, Grolier, et al., 1986 | DH |
176.69 | 298.15 | Tanaka, Toyama, et al., 1986 | DH |
177.08 | 298.15 | Zegers and Somsen, 1984 | DH |
174.3 | 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 |
181.6 | 303.5 | Griigo'ev, Yanin, et al., 1979 | T = 303 to 462 K. p = 0.98 bar.; DH |
179.5 | 301.2 | Paz Andrade, Paz, et al., 1970 | T = 28, 40°C.; DH |
177.03 | 298.15 | Counsell, Hales, et al., 1965 | T = 11 to 323 K.; DH |
189.1 | 323. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 21 to 78°C.; DH |
215.5 | 302.6 | Phillip, 1939 | DH |
183.3 | 298. | Trew and Watkins, 1933 | DH |
175.3 | 294.0 | Parks, 1925 | T = 90 to 294 K. Value is unsmoothed experimental datum.; DH |
180.3 | 303. | Willams and Daniels, 1924 | T = 303 to 343 K. Equation only.; DH |
174.5 | 298. | von Reis, 1881 | T = 290 to 390 K.; 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
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. | bar | 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° | 52. ± 3. | kJ/mol | AVG | N/A | Average of 15 out of 16 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
43.29 | 390.9 | N/A | Majer and Svoboda, 1985 | |
46.0 | 372. | EB | Muñoz and Krähenbühl, 2001 | Based on data from 357. to 389. K.; AC |
38.2 | 423. | N/A | Wormald and Fennell, 2000 | AC |
29.6 | 473. | N/A | Wormald and Fennell, 2000 | AC |
20.8 | 523. | N/A | Wormald and Fennell, 2000 | AC |
49.9 | 330. | N/A | Dejoz, Cruz Burguet, et al., 1995 | Based on data from 315. to 390. K.; AC |
45.3 | 379. | N/A | Susial and Ortega, 1993 | Based on data from 364. to 403. K.; AC |
45.3 | 387. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 399. K.; AC |
50.1 | 338. | A | Stephenson and Malanowski, 1987 | Based on data from 323. to 413. K.; AC |
41.9 | 428. | A | Stephenson and Malanowski, 1987 | Based on data from 413. to 550. K.; AC |
51.6 | 236. | A | Stephenson and Malanowski, 1987 | Based on data from 209. to 251. K.; AC |
45.4 | 386. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 397. K.; AC |
43.8 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 429. K.; AC |
41.9 | 430. | A | Stephenson and Malanowski, 1987 | Based on data from 415. to 501. K.; AC |
37.4 | 512. | A | Stephenson and Malanowski, 1987 | Based on data from 497. to 563. K.; AC |
47.2 | 366. | EB | Stephenson and Malanowski, 1987 | Based on data from 351. to 397. K. See also Ambrose, Counsell, et al., 1970.; AC |
49.0 | 344. | N/A | Sachek, Peshchenko, et al., 1982 | Based on data from 329. to 391. K.; AC |
49.5 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
48.6 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
47.5 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
46.4 ± 0.1 | 363. | C | Svoboda, Veselý, et al., 1973 | AC |
55.0 | 303. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 288. to 404. K.; AC |
53.0 | 310. | DTA | Kemme and Kreps, 1969 | Based on data from 295. to 391. K.; AC |
47.2 ± 0.1 | 356. | C | Counsell, Hales, et al., 1965, 2 | AC |
45.4 ± 0.1 | 381. | C | Counsell, Hales, et al., 1965, 2 | AC |
43.1 ± 0.1 | 391. | C | Counsell, Hales, et al., 1965, 2 | AC |
42.1 | 434. | N/A | Ambrose and Townsend, 1963 | Based on data from 419. to 563. K.; AC |
46.6 | 377. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 362. to 398. K.; AC |
48.3 | 352. | N/A | Brown and Smith, 1959 | Based on data from 337. to 390. K. See also Boublik, Fried, et al., 1984.; AC |
48.3 | 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)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 298. to 410. |
---|---|
A (kJ/mol) | 62.53 |
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 (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
295.8 to 391.0 | 4.54607 | 1351.555 | -93.34 | Kemme and Kreps, 1969 | |
391. to 479. | 4.39031 | 1254.502 | -105.246 | Hessel and Geiseler, 1965 | Coefficents calculated by NIST from author's data. |
419.34 to 562.98 | 4.42921 | 1305.001 | -94.676 | Ambrose and Townsend, 1963, 2 | Coefficents calculated by NIST from author's data. |
362.36 to 398.84 | 4.50393 | 1313.878 | -98.789 | Biddiscombe, Collerson, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.372 | 184.5 | Counsell, Hales, et al., 1965 | DH |
9.28 | 183.9 | Acree, 1991 | AC |
9.280 | 183.9 | Parks, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
50.79 | 184.5 | Counsell, Hales, et al., 1965 | DH |
50.46 | 183.9 | Parks, 1925 | DH |
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
RCD - Robert C. Dunbar
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
C4H9O- + =
By formula: C4H9O- + H+ = C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1570. ± 8.4 | kJ/mol | CIDC | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
ΔrH° | 1571. ± 8.8 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1569. ± 12. | kJ/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° | 1543. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
ΔrG° | 1543. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1541. ± 12. | kJ/mol | CIDC | Boand, Houriet, et al., 1983 | gas phase; value altered from reference due to change in acidity scale; B |
By formula: C4H11O+ + C4H10O = (C4H11O+ • C4H10O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 132. | kJ/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 129. | J/mol*K | N/A | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 93.3 | kJ/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M |
By formula: C3H9Si+ + C4H10O = (C3H9Si+ • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 185. | kJ/mol | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | N/A | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
124. | 468. | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M |
By formula: C3H9Sn+ + C4H10O = (C3H9Sn+ • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 153. | kJ/mol | PHPMS | Stone and Splinter, 1984 | gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 136. | J/mol*K | N/A | Stone and Splinter, 1984 | gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
81.6 | 525. | PHPMS | Stone and Splinter, 1984 | gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M |
By formula: CH6N+ + C4H10O = (CH6N+ • C4H10O)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 98.3 | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
44.4 | 495. | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
By formula: F- + C4H10O = (F- • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 135. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 108. | J/mol*K | N/A | Larson and McMahon, 1983 | gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 103. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
By formula: Cl- + C4H10O = (Cl- • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 73.6 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 97.1 | J/mol*K | N/A | Larson and McMahon, 1984 | gas phase; switching reaction(Cl-)CH3OH, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 44.8 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: Na+ + C4H10O = (Na+ • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 109. ± 5.0 | kJ/mol | CIDT | Rodgers and Armentrout, 1999 | RCD |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
82.4 | 298. | IMRE | McMahon and Ohanessian, 2000 | Anchor alanine=39.89; RCD |
By formula: C4H8O + H2 = C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -81.88 ± 0.75 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | liquid phase; ALS |
ΔrH° | -70.5 ± 1.3 | kJ/mol | Chyd | Buckley and Cox, 1967 | gas phase; ALS |
By formula: C6H5S- + C4H10O = (C6H5S- • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 61.1 | kJ/mol | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 105. | J/mol*K | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
By formula: C7H5NO + C4H10O = C11H15NO2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -83.9 ± 4.4 | kJ/mol | Cm | Pannone and Macosko, 1987 | liquid phase; ALS |
ΔrH° | -105. ± 1. | kJ/mol | Cm | Lovering and Laidler, 1962 | solid phase; ALS |
+ = C4H9D10FO-
By formula: F- + C4H10O = C4H9D10FO-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 101. ± 8.4 | kJ/mol | IMRE | Wilkinson, Szulejko, et al., 1992 | gas phase; Reported relative to ROH..F-, 0.5 kcal/mol weaker.; B |
By formula: Mg+ + C4H10O = (Mg+ • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 270. ± 20. | kJ/mol | ICR | Operti, Tews, et al., 1988 | gas phase; switching reaction,Thermochemical ladder(Mg+)CH3OH; M |
By formula: C4H10O + ClHO3S = C4H10O4S + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 58. ± 1. | kJ/mol | Cm | Markitanova, Barsukov, et al., 1981 | liquid phase; solvent: Dichloromethane; Sulfation; ALS |
By formula: C4H10O + C3H4O2 = C7H12O2 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16. | kJ/mol | Eqk | Selyakova, Vytnov, et al., 1976 | liquid phase; Heat of esterification 60-180 C; ALS |
By formula: C6H12O2 + H2O = C2H4O2 + C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.3 ± 0.2 | kJ/mol | Cm | Wadso, 1958 | liquid phase; Heat of hydrolysis; ALS |
By formula: C4H2O3 + C4H10O = C8H12O4
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -39. | kJ/mol | Kin | Merca, Poraicu, et al., 1978 | solid phase; solvent: n-Butanol; DTA; ALS |
By formula: C4H8 + C4H10O = C8H18O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -34.8 ± 2.7 | kJ/mol | Eqk | Sharonov, Mishentseva, et al., 1991 | liquid phase; ALS |
By formula: C2H2O + C4H10O = C6H12O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -146.9 | kJ/mol | Cm | Rice and Greenberg, 1934 | liquid phase; ALS |
By formula: Li+ + C4H10O = (Li+ • C4H10O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 178. ± 7.9 | kJ/mol | CIDT | Rodgers and Armentrout, 2000 | RCD |
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 |
---|---|---|---|---|
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. |
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.
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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,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions T Temperature 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 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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