2-Butanone
- Formula: C4H8O
- Molecular weight: 72.1057
- IUPAC Standard InChIKey: ZWEHNKRNPOVVGH-UHFFFAOYSA-N
- CAS Registry Number: 78-93-3
- 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: Butan-2-one; Butanone; Ethyl methyl ketone; Ketone, methyl ethyl; Methyl ethyl ketone; MEK; C2H5COCH3; Acetone, methyl-; Aethylmethylketon; 3-Butanone; Butanone 2; Ethyl methyl cetone; Ethylmethylketon; Ketone, ethyl methyl; Meetco; Methyl acetone; Metiletilchetone; Metyloetyloketon; Rcra waste number U159; UN 1193; 2-Oxobutane; 2-Butanal; 2-butanone (MEK; methyl ethyl ketone); 2-butanone (MEK)
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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:
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 | -238.6 ± 0.84 | kJ/mol | Cm | Chao and Zwolinski, 1976 | ALS |
ΔfH°gas | -238.7 ± 0.96 | kJ/mol | Eqk | Buckley and Herington, 1965 | Reanalyzed by Cox and Pilcher, 1970, Original value = -238.0 kJ/mol; ALS |
ΔfH°gas | -238.1 | kJ/mol | Ccb | Sinke and Oetting, 1964 | ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
57.03 | 100. | Chao J., 1986 | p=1 bar. Recommended values agree with results of statistical calculations [ Sinke G.C., 1964, Chao J., 1976] within 0.2-1.8 J/mol*K. S(T) values calculated by [ Nickerson J.K., 1961] are different from selected ones by 4-5 J/mol*K.; GT |
68.98 | 150. | ||
80.20 | 200. | ||
96.12 | 273.15 | ||
101.68 ± 0.14 | 298.15 | ||
102.09 | 300. | ||
124.37 | 400. | ||
145.05 | 500. | ||
163.15 | 600. | ||
178.77 | 700. | ||
192.25 | 800. | ||
203.91 | 900. | ||
213.99 | 1000. | ||
222.69 | 1100. | ||
230.21 | 1200. | ||
236.70 | 1300. | ||
242.31 | 1400. | ||
247.17 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
113.43 ± 0.23 | 347.15 | von Geiseler G., 1973 | Experimental data [ Vilcu R., 1975] differ appreciably from data selected here. Their correctness seems to be doubtful (see [ Kabo G.J., 1995]). Low accuracy is also expected for experimental value of Cp(410 K)=123.85 J/mol*K [ Bennewitz K., 1938]. Please also see Nickerson J.K., 1961.; GT |
115.65 ± 0.17 | 358.79 | ||
118.70 ± 0.18 | 371.90 | ||
119.03 ± 0.24 | 372.15 | ||
121.75 ± 0.18 | 385.60 | ||
124.39 ± 0.25 | 397.15 | ||
124.60 ± 0.19 | 399.55 | ||
126.98 ± 0.19 | 410.70 | ||
131.71 ± 0.26 | 432.15 | ||
138.62 ± 0.28 | 467.15 |
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 | -273.3 ± 1.2 | kJ/mol | Ccb | Sinke and Oetting, 1964 | ALS |
ΔfH°liquid | -279.0 | kJ/mol | Ccb | Parks, Mosley, et al., 1950 | see Moore, Renquist, et al., 1940; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2444.2 | kJ/mol | Ccb | Sinke and Oetting, 1964 | Corresponding ΔfHºliquid = -273.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2438.4 | kJ/mol | Ccb | Parks, Mosley, et al., 1950 | see Moore, Renquist, et al., 1940; Corresponding ΔfHºliquid = -278.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2436.3 ± 1.5 | kJ/mol | Ccb | Crog and Hunt, 1942 | Corresponding ΔfHºliquid = -281.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 239.0 | J/mol*K | N/A | Andon, Counsell, et al., 1968 | DH |
S°liquid | 238.82 | J/mol*K | N/A | Sinke and Oetting, 1964 | DH |
S°liquid | 241.4 | J/mol*K | N/A | Parks, Kennedy, et al., 1956 | Extrapolation below 80 K, 53.47 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
159. | 298.15 | Malhotra and Woolf, 1992 | T = 278 to 338 K. p = 0.1 MPa.; DH |
162.2 | 303.15 | Reddy, 1986 | T = 303.15, 313.15 K.; DH |
158.4 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
158.4 | 298.15 | Costas and Patterson, 1985, 2 | DH |
157.91 | 298.15 | Grolier and Benson, 1984 | DH |
158.4 | 298.1 | Roux, Perron, et al., 1978 | T = 277 to 313 K.; DH |
159.2 | 298.15 | Grolier, Benson, et al., 1975 | DH |
158.7 | 298.15 | Andon, Counsell, et al., 1968 | T = 10 to 320 K.; DH |
158.0 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 353 K.; DH |
158.91 | 298.15 | Sinke and Oetting, 1964 | T = 13 to 308 K.; DH |
158.41 | 298.15 | Parks, Kennedy, et al., 1956 | T = 80 to 300 K.; DH |
160.7 | 297.0 | Kolosovskii and Udovenko, 1934 | DH |
160.7 | 297.0 | de Kolossowsky and Udowenko, 1933 | 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 353. ± 1. | K | AVG | N/A | Average of 88 out of 89 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 186.4 ± 0.5 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 186.5 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 186.47 | K | N/A | Andon, Counsell, et al., 1968, 2 | Uncertainty assigned by TRC = 0.04 K; TRC |
Ttriple | 186.4 | K | N/A | Sinke and Oetting, 1964, 2 | Uncertainty assigned by TRC = 0.06 K; measured for the sample, 1/f = 1.00; TRC |
Ttriple | 186.48 | K | N/A | Sinke and Oetting, 1964, 2 | Uncertainty assigned by TRC = 0.03 K; measured for the sample, 1/f = 1.00; TRC |
Ttriple | 186.1 | K | N/A | Parks, Kennedy, et al., 1956, 2 | Uncertainty assigned by TRC = 0.1 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 535. ± 2. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 42. ± 2. | bar | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.74 | mol/l | N/A | Kobe, Crawford, et al., 1955 | Uncertainty assigned by TRC = 0.21 mol/l; TRC |
ρc | 3.49 | mol/l | N/A | Rosenbaum, 1951 | Uncertainty assigned by TRC = 0.06 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 34. ± 2. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
31.3 | 352.8 | N/A | Majer and Svoboda, 1985 | |
34.6 | 309. | A | Stephenson and Malanowski, 1987 | Based on data from 294. to 342. K.; AC |
32.5 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. to 403. K.; AC |
31.6 | 412. | A | Stephenson and Malanowski, 1987 | Based on data from 397. to 479. K.; AC |
31.1 | 488. | A | Stephenson and Malanowski, 1987 | Based on data from 473. to 537. K.; AC |
33.9 | 330. | A,EB,GS | Stephenson and Malanowski, 1987 | Based on data from 315. to 363. K. See also Ambrose, Ellender, et al., 1975 and Collerson, Counsell, et al., 1965.; AC |
35.6 | 273. | N/A | Di Cave, Chianese, et al., 1978 | Based on data from 258. to 362. K.; AC |
33.8 | 315. | C | Geiseler, Quitzsch, et al., 1973 | AC |
33.8 ± 0.1 | 314. | C | Nickerson, Kobe, et al., 1961 | AC |
32.3 ± 0.1 | 338. | C | Nickerson, Kobe, et al., 1961 | AC |
31.3 ± 0.1 | 352. | C | Nickerson, Kobe, et al., 1961 | AC |
30.5 ± 0.1 | 363. | C | Nickerson, Kobe, et al., 1961 | AC |
30.0 ± 0.1 | 370. | C | Nickerson, Kobe, et al., 1961 | AC |
33.9 | 329. | N/A | Stull, 1947 | Based on data from 314. to 370. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 371. | 51.87 | 0.2925 | 536.8 | 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 |
---|---|---|---|---|---|
314.6 to 370.6 | 3.9894 | 1150.207 | -63.904 | Nickerson, Kobe, et al., 1961 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.385 | 186.47 | Andon, Counsell, et al., 1968 | DH |
8.4387 | 186.48 | Sinke and Oetting, 1964 | DH |
8.44 | 186.5 | Acree, 1991 | AC |
8.485 | 186.1 | Parks, Kennedy, et al., 1956 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
44.98 | 186.47 | Andon, Counsell, et al., 1968 | DH |
45.25 | 186.48 | Sinke and Oetting, 1964 | DH |
45.59 | 186.1 | Parks, Kennedy, et al., 1956 | 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:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
RCD - Robert C. Dunbar
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: C4H9O+ + C4H8O = (C4H9O+ • C4H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 127. | 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, Keesee and Castleman, 1986; 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, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 88.7 | 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, Keesee and Castleman, 1986; M |
By formula: C5H11O+ + C4H8O = (C5H11O+ • C4H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 123. | 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, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | 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, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 86.6 | 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, Keesee and Castleman, 1986; M |
C4H7O- + =
By formula: C4H7O- + H+ = C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1536. ± 12. | kJ/mol | G+TS | Chyall, Brickhouse, et al., 1994 | gas phase; Primary and secondary sites are of equal acidity by equilibration. Acidity from Zimmerman, Reed, et al., 1977; B |
ΔrH° | 1545. ± 10. | kJ/mol | D-EA | Zimmerman, Reed, et al., 1977 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1508. ± 11. | kJ/mol | IMRE | Chyall, Brickhouse, et al., 1994 | gas phase; Primary and secondary sites are of equal acidity by equilibration. Acidity from Zimmerman, Reed, et al., 1977; B |
ΔrG° | 1516. ± 11. | kJ/mol | H-TS | Zimmerman, Reed, et al., 1977 | gas phase; B |
By formula: C3H9Sn+ + C4H8O = (C3H9Sn+ • C4H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 164. | 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° | 137. | 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 |
---|---|---|---|---|
92.5 | 525. | PHPMS | Stone and Splinter, 1984 | gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M |
By formula: CH6N+ + C4H8O = (CH6N+ • C4H8O)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 105. | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 100. | 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 |
---|---|---|---|---|
47.7 | 553. | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
By formula: Cl- + C4H8O = (Cl- • C4H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 61.9 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 87.9 | J/mol*K | N/A | Larson and McMahon, 1984 | gas phase; switching reaction(Cl-)(CH3)2CO, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 36. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: H2 + C4H8O = C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -54.18 | kJ/mol | Eqk | Buckley and Herington, 1965 | gas phase; ALS |
ΔrH° | -54.3 ± 0.4 | kJ/mol | Chyd | Dolliver, Gresham, et al., 1938 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -55.2 ± 0.4 kJ/mol; At 355 °K; ALS |
C4H7O- + =
By formula: C4H7O- + H+ = C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1678. ± 17. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | <1711.3 | kJ/mol | CIDT | Graul and Squires, 1988 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1646. ± 17. | kJ/mol | H-TS | Graul and Squires, 1990 | gas phase; B |
By formula: NO- + C4H8O = (NO- • C4H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 177. | kJ/mol | ICR | Reents and Freiser, 1981 | gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978; M |
C4H7O- + =
By formula: C4H7O- + H+ = C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1540. ± 12. | kJ/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1512. ± 8.4 | kJ/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
(CAS Reg. No. 35730-33-7 • 4294967295) + = CAS Reg. No. 35730-33-7
By formula: (CAS Reg. No. 35730-33-7 • 4294967295C4H8O) + C4H8O = CAS Reg. No. 35730-33-7
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 164. ± 9.2 | kJ/mol | N/A | Taft, 1987 | gas phase; value altered from reference due to change in acidity scale; B |
By formula: C4H10O = H2 + C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 54.22 | kJ/mol | Eqk | Cubberley and Mueller, 1946 | gas phase; ALS |
ΔrH° | 57.170 | kJ/mol | Eqk | Kolb and Burwell, 1945 | gas phase; ALS |
By formula: Mg+ + C4H8O = (Mg+ • C4H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 280. | kJ/mol | ICR | Operti, Tews, et al., 1988 | gas phase; switching reaction,Thermochemical ladder(CH3OH); M |
By formula: C6H14O2 + H2O = 2CH4O + C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19.33 ± 0.04 | kJ/mol | Cm | Wiberg and Squires, 1979 | liquid phase; Heat of hydrolysis; ALS |
By formula: HI + C4H7IO = I2 + C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -42.7 | kJ/mol | Kin | Solly, Golden, et al., 1970 | gas phase; ALS |
By formula: H2 + C4H6O = C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -550.6 | kJ/mol | Chyd | Veselova and Sul'man, 1980 | liquid phase; ALS |
By formula: Na+ + C4H8O = (Na+ • C4H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 131. ± 7.1 | kJ/mol | CIDT | Moision and Armentrout, 2002 | 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 |
---|---|---|---|---|
20. | 5000. | L | N/A | |
20. | 5000. | M | N/A | The data from Table 1 by missing citation was used to redo the regression analysis. The data for acetone in their Table 2 is wrong. |
7.7 | X | N/A | Value given here as cited in missing citation. | |
6.8 | -5200. | X | N/A | |
4.1 to 7.7 | X | Howe, Mullins, et al., 1987 | Value given here as quoted by missing citation. | |
7.1 | 5800. | X | N/A | |
18. | 5700. | M | N/A | |
10. | M | N/A | Value at T = 303. K. | |
18. | M | N/A | ||
17. | X | N/A | Value given here as quoted by missing citation. | |
19. | M | N/A | ||
21. | M | Buttery, Ling, et al., 1969 | ||
7.1 | R | 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.
Chao and Zwolinski, 1976
Chao, J.; Zwolinski, B.J.,
Ideal gas thermodynamic properties of propanone and 2-butanone,
J. Phys. Chem. Ref. Data, 1976, 5, 319-328. [all data]
Buckley and Herington, 1965
Buckley, E.; Herington, E.F.G.,
Equilibria in some secondary alcohol + hydrogen + ketone systems,
Trans. Faraday Soc., 1965, 61, 1618-1625. [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]
Sinke and Oetting, 1964
Sinke, G.C.; Oetting, F.L.,
The chemical thermodynamic properties of methyl ethyl ketone,
J. Phys. Chem., 1964, 68, 1354-1358. [all data]
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]
Sinke G.C., 1964
Sinke G.C.,
The chemical thermodynamic properties of methyl ethyl ketone,
J. Phys. Chem., 1964, 68, 1354-1358. [all data]
Chao J., 1976
Chao J.,
Ideal gas thermodynamic properties of propanone and 2-butanone,
J. Phys. Chem. Ref. Data, 1976, 5, 319-328. [all data]
Nickerson J.K., 1961
Nickerson J.K.,
The thermodynamic properties of the methyl ketone series,
J. Phys. Chem., 1961, 65, 1037-1043. [all data]
von Geiseler G., 1973
von Geiseler G.,
The heat capacity and the heat of vaporization of isomeric butylmethylketones and propylacetates,
Z. Phys. Chem. (Leipzig), 1973, 252, 170-176. [all data]
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Notes
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- 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°liquid Entropy of liquid at standard conditions T Temperature 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 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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