Isopropyl Alcohol
- Formula: C3H8O
- Molecular weight: 60.0950
- IUPAC Standard InChIKey: KFZMGEQAYNKOFK-UHFFFAOYSA-N
- CAS Registry Number: 67-63-0
- 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: 2-Propanol; sec-Propyl Alcohol; Alcojel; Alcosolve 2; Avantin; Avantine; Combi-Schutz; Dimethylcarbinol; Hartosol; Imsol A; Isohol; Isopropanol; Lutosol; Petrohol; Propol; PRO; Takineocol; 1-Methylethyl Alcohol; iso-C3H7OH; 2-Hydroxypropane; Propane, 2-hydroxy-; sec-Propanol; Propan-2-ol; i-Propylalkohol; Alcolo; Alcool isopropilico; Alcool isopropylique; Alkolave; Arquad DMCB; iso-Propylalkohol; Isopropyl alcohol, rubbing; IPA; Lavacol; Visco 1152; Alcosolve; i-Propanol; 2-Propyl alcohol; Spectrar; Sterisol hand disinfectant; UN 1219; n-Propan-2-ol; 1-methylethanol; Propanol-2; Virahol; IPS 1
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry 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 as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -272.8 | kJ/mol | Eqk | Buckley and Herington, 1965 | ALS |
ΔfH°gas | -271.1 | kJ/mol | N/A | Chao and Rossini, 1965 | Value computed using ΔfHliquid° value of -317.0±0.3 kj/mol from Chao and Rossini, 1965 and ΔvapH° value of 45.9 kj/mol from Snelson and Skinner, 1961.; DRB |
ΔfH°gas | -272.3 ± 0.92 | kJ/mol | Ccb | Snelson and Skinner, 1961 | ALS |
ΔfH°gas | -272.8 | kJ/mol | N/A | Parks, Mosley, et al., 1950 | Value computed using ΔfHliquid° value of -318.7 kj/mol from Parks, Mosley, et al., 1950 and ΔvapH° value of 45.9 kj/mol from Snelson and Skinner, 1961.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.32 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Discrepancies with other statistically calculated values [ Green J.H.S., 1963] and [51KOB] increase at high temperatures up to 5 and 9 J/mol*K, respectively, in Cp(T). There is a good agreement with results [ Chao J., 1986]. Please also see Chao J., 1986, 2.; GT |
46.04 | 100. | ||
57.98 | 150. | ||
68.28 | 200. | ||
83.72 | 273.15 | ||
89.32 ± 0.15 | 298.15 | ||
89.74 | 300. | ||
112.15 | 400. | ||
131.96 | 500. | ||
148.30 | 600. | ||
161.75 | 700. | ||
173.04 | 800. | ||
182.67 | 900. | ||
190.97 | 1000. | ||
198.16 | 1100. | ||
204.41 | 1200. | ||
209.85 | 1300. | ||
214.60 | 1400. | ||
218.75 | 1500. | ||
227.0 | 1750. | ||
233.1 | 2000. | ||
237.6 | 2250. | ||
241.0 | 2500. | ||
243.7 | 2750. | ||
245.7 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
103.06 | 358.72 | 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 1.59 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Other experimental values of Cp [ Parks G.S., 1940] (118.83 at 427.9 K, 127.61 at 457.7 K, and 135.56 J/mol*K at 480.3 K) are believed to be less reliable. Please also see Hales J.L., 1963, Berman N.S., 1964.; GT |
105.7 ± 1.6 | 365.75 | ||
105.77 | 371.15 | ||
106.29 | 373.15 | ||
108.1 ± 1.6 | 378.85 | ||
109.2 ± 1.6 | 384.95 | ||
110.08 | 391.15 | ||
110.8 ± 1.6 | 393.65 | ||
111.65 | 398.15 | ||
113.0 ± 1.6 | 405.35 | ||
114.35 | 411.15 | ||
117.02 | 423.15 | ||
118.70 | 431.15 | ||
122.10 | 448.15 | ||
122.80 | 451.15 | ||
121.7 ± 1.6 | 453.15 | ||
124.2 ± 1.6 | 466.75 | ||
127.01 | 473.15 | ||
126.7 ± 1.6 | 480.55 | ||
130.3 ± 1.6 | 499.75 | ||
132.9 ± 1.6 | 513.95 | ||
137.5 ± 1.6 | 539.05 | ||
142.6 ± 1.6 | 567.05 | ||
148.1 ± 1.6 | 597.25 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry 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 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 | -317.0 ± 0.3 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; ALS |
ΔfH°liquid | -318.2 ± 0.71 | kJ/mol | Ccb | Snelson and Skinner, 1961 | ALS |
ΔfH°liquid | -318.7 | kJ/mol | Ccb | Parks, Mosley, et al., 1950 | see Parks and Moore, 1939; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2006.9 ± 0.2 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; Corresponding ΔfHºliquid = -316.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2005.8 ± 0.4 | kJ/mol | Ccb | Snelson and Skinner, 1961 | Corresponding ΔfHºliquid = -318.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2005.1 | kJ/mol | Ccb | Parks, Mosley, et al., 1950 | see Parks and Moore, 1939; Corresponding ΔfHºliquid = -318.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 180.58 | J/mol*K | N/A | Andon, Counsell, et al., 1963 | DH |
S°liquid | 179.9 | J/mol*K | N/A | Kelley, 1929 | DH |
S°liquid | 192.9 | J/mol*K | N/A | Parks and Kelley, 1928 | Extrapolation below 70 K, 43.56 J/mol*K.; DH |
S°liquid | 190.8 | J/mol*K | N/A | Parks and Kelley, 1925 | Extrapolation below 90 K, 53.22 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
161.2 | 298.15 | Roux, Roberts, et al., 1980 | DH |
154.75 | 298.15 | Brown and Ziegler, 1979 | T = 185 to 304 K. Results as equation only.; DH |
165.6 | 311.6 | Griigo'ev, Yanin, et al., 1979 | T = 311 to 453 K. p = 0.98 bar.; DH |
154.43 | 298.15 | Andon, Counsell, et al., 1963 | T = 10 to 330 K.; DH |
162.8 | 298.2 | Katayama, 1962 | T = 10 to 60°C.; DH |
180.3 | 324. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 21 to 81°C.; DH |
154.0 | 298. | Ginnings and Corruccini, 1948 | T = 0 to 200°C.; DH |
159.99 | 298.04 | Zhdanov, 1945 | T = 7 to 41°C. Value is unsmoothed experimental datum.; DH |
172.4 | 303.2 | Phillip, 1939 | DH |
163.6 | 298. | Trew and Watkins, 1933 | DH |
149.75 | 292.84 | Kelley, 1929 | T = 16 to 298 K. Value is unsmoothed experimental datum.; DH |
180.3 | 298.1 | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 42.68 J/mol*K.; DH |
151.0 | 293.1 | Parks and Kelley, 1928 | T = 71 to 293 K. Value is unsmoothed experimental datum.; DH |
152.3 | 293.1 | Parks and Kelley, 1925 | T = 71 to 293 K. Value is unsmoothed experimental datum.; DH |
169.9 | 303. | Willams and Daniels, 1924 | T = 303 to 323 K. Equation only.; DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase 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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
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
C3H7O- + =
By formula: C3H7O- + H+ = C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1569. ± 4.2 | kJ/mol | D-EA | Ramond, Davico, et al., 2000 | gas phase; 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° | 1576. ± 4.2 | kJ/mol | CIDT | DeTuri and Ervin, 1999 | gas phase; B |
ΔrH° | 1572. ± 8.4 | kJ/mol | CIDC | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1542. ± 4.6 | kJ/mol | H-TS | Ramond, Davico, et al., 2000 | gas phase; 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° | 1544. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
By formula: Cl- + C3H8O = (Cl- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 81.17 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrH° | 76.6 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
ΔrH° | 73.6 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 103. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
ΔrS° | 97.1 | J/mol*K | N/A | Larson and McMahon, 1984 | gas phase; switching reaction(cl-)t-C4H9OH, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 47.36 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 45.61 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
ΔrG° | 44.8 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: C2H7O+ + C3H8O = (C2H7O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 133. | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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° | 124. | J/mol*K | N/A | Bomse and Beauchamp, 1981 | 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° | 96.7 | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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: C3H9O+ + C3H8O = (C3H9O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 133. | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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° | 124. | J/mol*K | N/A | Bomse and Beauchamp, 1981 | 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° | 96.7 | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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: C4H11O+ + C3H8O = (C4H11O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 128. | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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° | 118. | J/mol*K | N/A | Bomse and Beauchamp, 1981 | 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° | 92.5 | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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: C4H11O+ + C3H8O = (C4H11O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 134. | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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° | 115. | J/mol*K | N/A | Bomse and Beauchamp, 1981 | 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° | 99.6 | kJ/mol | ICR | Bomse and Beauchamp, 1981 | 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: CN- + C3H8O = (CN- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 69.9 ± 3.3 | kJ/mol | TDAs | Larson, Szulejko, et al., 1988 | gas phase; B,M |
ΔrH° | 76. ± 15. | kJ/mol | IMRE | Larson and McMahon, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | PHPMS | Larson, Szulejko, et al., 1988 | gas phase; M |
ΔrS° | 104. | J/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° | 37.7 ± 0.84 | kJ/mol | TDAs | Larson, Szulejko, et al., 1988 | gas phase; B |
ΔrG° | 44.8 ± 9.6 | kJ/mol | IMRE | Larson and McMahon, 1987 | gas phase; B,M |
By formula: F- + C3H8O = (F- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 140.2 ± 2.9 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrH° | 135. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
ΔrH° | 139. ± 9.2 | kJ/mol | CIDT | DeTuri and Ervin, 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 107. | 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° | 107.5 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 103. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
By formula: C3H9Si+ + C3H8O = (C3H9Si+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 184. | 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° | 129. | 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 |
---|---|---|---|---|
123. | 468. | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M |
By formula: (Cl- • 2C3H8O) + C3H8O = (Cl- • 3C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 62.3 ± 2.1 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrH° | 52.3 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 109. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 22.2 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 20. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • C3H8O) + C3H8O = (Cl- • 2C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 69.9 ± 1.3 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrH° | 65.3 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 105. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 32.1 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 34. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • 7C3H8O) + C3H8O = (Cl- • 8C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.6 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; Estimated entropy; single temperature measurement; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | N/A | Hiraoka and Mizuse, 1987 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 6.7 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; Estimated entropy; single temperature measurement; B |
By formula: I- + C3H8O = (I- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 54.81 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrH° | 51.0 ± 4.2 | kJ/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 79.9 | J/mol*K | PHPMS | Caldwell and Kebarle, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 26.5 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 27. ± 4.2 | kJ/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B |
By formula: H2 + C3H6O = C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -68.74 ± 0.42 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | liquid phase; ALS |
ΔrH° | -55.23 | kJ/mol | Eqk | Buckley and Herington, 1965 | gas phase; ALS |
ΔrH° | -55.40 ± 0.42 | kJ/mol | Chyd | Dolliver, Gresham, et al., 1938 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -56.1 ± 0.4 kJ/mol; At 355 °K; ALS |
+ = C3H8BrO-
By formula: Br- + C3H8O = C3H8BrO-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.25 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 34.9 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
ΔrG° | 38. ± 8.4 | kJ/mol | IMRE | Tanabe, Morgon, et al., 1996 | gas phase; Anchored to H2O..Br- of Hiraoka, Mizure, et al., 19882; B |
By formula: Na+ + C3H8O = (Na+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 113. ± 4.2 | kJ/mol | CIDT | Armentrout and Rodgers, 2000 | RCD |
ΔrH° | 113. ± 4.6 | kJ/mol | CIDT | Rodgers and Armentrout, 1999 | RCD |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
85.4 | 298. | IMRE | McMahon and Ohanessian, 2000 | Anchor alanine=39.89; RCD |
0.0 | 0. | CIDT | Rodgers and Armentrout, 1999 | RCD |
By formula: (Cl- • 3C3H8O) + C3H8O = (Cl- • 4C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 49.8 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 14. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • 4C3H8O) + C3H8O = (Cl- • 5C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 48.5 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 128. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 10. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • 5C3H8O) + C3H8O = (Cl- • 6C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 47.3 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 8.4 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • 6C3H8O) + C3H8O = (Cl- • 7C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.4 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 131. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 7.1 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: CH3S- + C3H8O = (CH3S- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 71.55 ± 0.84 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 96.7 | J/mol*K | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 42.7 ± 3.3 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
+ 2 = C6H16FO2-
By formula: F- + 2C3H8O = C6H16FO2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 87.03 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 55.48 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
+ = C9H13OS-
By formula: C6H5S- + C3H8O = C9H13OS-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 62.76 ± 0.42 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 30.5 ± 1.7 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
+ 3 = C9H24FO3-
By formula: F- + 3C3H8O = C9H24FO3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 73.64 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 35.0 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
+ 2 = C6H16IO2-
By formula: I- + 2C3H8O = C6H16IO2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.0 ± 1.3 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 19.5 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
+ 2 = C6H16BrO2-
By formula: Br- + 2C3H8O = C6H16BrO2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 51.46 ± 0.84 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 22.8 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
+ 3 = C9H24IO3-
By formula: I- + 3C3H8O = C9H24IO3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 39.7 ± 2.9 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 14.8 | kJ/mol | TDAs | Bogdanov, Peschke, et al., 1999 | gas phase; B |
By formula: C4H8 + C3H8O = C7H16O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -22.9 ± 1.3 | kJ/mol | Eqk | Calderon, Tejero, et al., 1997 | liquid phase; ALS |
ΔrH° | -21.7 ± 1.6 | kJ/mol | Cm | Sola, Pericas, et al., 1997 | liquid phase; ALS |
By formula: C3H8O = H2 + C3H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 55.23 | kJ/mol | Eqk | Buckley and Herington, 1965 | gas phase; ALS |
ΔrH° | 56.543 | kJ/mol | Eqk | Kolb and Burwell, 1945 | gas phase; ALS |
+ = C3H7D8FO-
By formula: F- + C3H8O = C3H7D8FO-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 102. ± 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+ + C3H8O = (Mg+ • C3H8O)
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: C5H10O2 + H2O = C2H4O2 + C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.3 ± 0.2 | kJ/mol | Cm | Wadso, 1958 | liquid phase; Heat of Hydrolysis; ALS |
By formula: C3H8O + C2HCl3O = 2,2,2-trichloro-1-isopropoxyethanol
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -41.6 | kJ/mol | Eqk | Jensen and Pedersen, 1971 | liquid phase; solvent: Heptane; ALS |
By formula: C6H12O + C3H6O = C6H10O + C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.9 ± 1.9 | kJ/mol | Eqk | Fedoseenko, Yursha, et al., 1983 | gas phase; At 503 K; ALS |
+ = C5H8Cl2F2O
By formula: C3H8O + C2Cl2F2 = C5H8Cl2F2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -183. ± 1. | kJ/mol | Eqk | Kennedy, Lacher, et al., 1969 | gas phase; ALS |
By formula: C6H10O + C3H8O = C6H12O + C3H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -9.9 ± 1.9 | kJ/mol | Eqk | Kabo, Yursha, et al., 1988 | gas phase; ALS |
By formula: C3H8O + HNO3 = C3H7NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -23.4 | kJ/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
By formula: C2H2O + C3H8O = C5H10O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -150.2 | kJ/mol | Cm | Rice and Greenberg, 1934 | liquid phase; ALS |
By formula: Li+ + C3H8O = (Li+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 173. ± 7.9 | kJ/mol | CIDT | Rodgers and Armentrout, 2000 | RCD |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry 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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Rice and Greenberg, 1934
Rice, F.O.; Greenberg, J.,
Ketene. III. Heat of formation and heat of reaction with alcohols,
J. Am. Chem. Soc., 1934, 38, 2268-2270. [all data]
Rodgers and Armentrout, 2000
Rodgers, M.T.; Armentrout, P.B.,
Noncovalent Metal-Ligand Bond Energies as Studied by Threshold Collision-Induced Dissociation,
Mass Spectrom. Rev., 2000, 19, 4, 215, https://doi.org/10.1002/1098-2787(200007)19:4<215::AID-MAS2>3.0.CO;2-X
. [all data]
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 S°liquid Entropy of liquid at standard conditions T Temperature 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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