1-Propanol
- Formula: C3H8O
- Molecular weight: 60.0950
- IUPAC Standard InChIKey: BDERNNFJNOPAEC-UHFFFAOYSA-N
- CAS Registry Number: 71-23-8
- 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: Propyl alcohol; n-Propan-1-ol; n-Propanol; n-Propyl alcohol; Ethylcarbinol; Optal; Osmosol extra; Propanol; Propylic alcohol; 1-Propyl alcohol; n-C3H7OH; 1-Hydroxypropane; Propanol-1; Propan-1-ol; n-Propyl alkohol; Alcool propilico; Alcool propylique; Propanole; Propanolen; Propanoli; Propylowy alkohol; UN 1274; Propylan-propyl alcohol; NSC 30300; Alcohol, propyl
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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 | -256. ± 3. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 322.49 | J/mol*K | N/A | Chao J., 1986 | Other values based on low-temperature thermal measurements are: 321.6 [ Buckley E., 1967], 321.7 [ Counsell J.F., 1968], 322.59 [ Green J.H.S., 1961], 323.42 [ Chermin H.A.G., 1961], and 324.72 J/mol*K [ Wilhoit R.C., 1973].; GT |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
40.58 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Discrepancies with other statistically calculated S(T) and Cp(T) values [ Green J.H.S., 1961, Mathews J.F., 1961, Chao J., 1986, 2], [ Chermin H.A.G., 1961], and [ Kobe K.A., 1951, Zhuravlev E.Z., 1959] amount up to 2.5, 4, and 7 J/mol*K, respectively. Please also see Chao J., 1986.; GT |
51.53 | 100. | ||
58.92 | 150. | ||
66.37 | 200. | ||
80.19 | 273.15 | ||
85.56 ± 0.14 | 298.15 | ||
85.96 | 300. | ||
108.03 | 400. | ||
128.19 | 500. | ||
145.41 | 600. | ||
160.05 | 700. | ||
172.62 | 800. | ||
183.51 | 900. | ||
192.97 | 1000. | ||
201.22 | 1100. | ||
208.40 | 1200. | ||
214.67 | 1300. | ||
220.14 | 1400. | ||
224.93 | 1500. | ||
234.5 | 1750. | ||
241.4 | 2000. | ||
246.6 | 2250. | ||
250.5 | 2500. | ||
254. | 2750. | ||
256. | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
102.26 ± 0.20 | 371.2 | 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 0.96 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see Mathews J.F., 1961.; GT |
107.28 ± 0.96 | 375.45 | ||
108.67 ± 0.96 | 383.05 | ||
109.42 ± 0.96 | 387.15 | ||
106.44 ± 0.21 | 391.2 | ||
111.21 ± 0.96 | 396.95 | ||
113.59 ± 0.96 | 409.95 | ||
110.42 ± 0.22 | 411.2 | ||
115.56 ± 0.96 | 420.75 | ||
115.97 ± 0.96 | 422.95 | ||
114.35 ± 0.23 | 431.2 | ||
118.71 ± 0.96 | 437.95 | ||
118.62 ± 0.24 | 451.2 | ||
122.94 ± 0.96 | 461.05 | ||
125.55 ± 0.96 | 475.35 | ||
130.97 ± 0.96 | 504.95 | ||
132.23 ± 0.96 | 511.85 | ||
135.98 ± 0.96 | 532.35 | ||
141.05 ± 0.96 | 560.05 | ||
144.49 ± 0.96 | 578.85 | ||
148.95 ± 0.96 | 603.25 |
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 | -302.54 ± 0.25 | kJ/mol | Ccb | Mosselman and Dekker, 1975 | ALS |
ΔfH°liquid | -303.0 ± 1.3 | kJ/mol | Eqk | Connett, 1972 | ALS |
ΔfH°liquid | -304.6 ± 0.4 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; ALS |
ΔfH°liquid | -302.5 ± 4.2 | kJ/mol | Ccb | Snelson and Skinner, 1961 | ALS |
ΔfH°liquid | -306.3 ± 1.0 | kJ/mol | Ccb | Green, 1960 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2021.31 ± 0.25 | kJ/mol | Ccb | Mosselman and Dekker, 1975 | Corresponding ΔfHºliquid = -302.54 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2019.4 ± 0.3 | kJ/mol | Ccb | Chao and Rossini, 1965 | see Rossini, 1934; Corresponding ΔfHºliquid = -304.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2021.4 ± 0.75 | kJ/mol | Ccb | Snelson and Skinner, 1961 | Corresponding ΔfHºliquid = -302.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2017.7 ± 1.0 | kJ/mol | Ccb | Green, 1960 | Corresponding ΔfHºliquid = -306.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2032.59 | kJ/mol | Ccb | Richards and Davis, 1920 | At 291 K; Corresponding ΔfHºliquid = -291.26 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 192.8 | J/mol*K | N/A | Counsell, Lees, et al., 1968 | DH |
S°liquid | 214.2 | J/mol*K | N/A | Parks and Huffman, 1926 | Extrapolation below 90 K, 64.85 J/mol*K.; DH |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 112.7 | J/mol*K | N/A | Counsell, Lees, et al., 1968 | glass phase; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
144.6 | 298. | Korolev, Kukharenko, et al., 1986 | DH |
143.96 | 298.15 | Tanaka, Toyama, et al., 1986 | DH |
144.44 | 298.15 | Zegers and Somsen, 1984 | DH |
138.40 | 288.15 | Benson and D'Arcy, 1982 | DH |
146.88 | 298.15 | Villamanan, Casanova, et al., 1982 | DH |
141.8 | 293.15 | Arutyunyan, Bagdasaryan, et al., 1981 | T = 293 to 353 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.360 kJ/kg*K. Cp given from 293.25 to 533.15 K for pressure range 10 to 60 MPa.; DH |
146.34 | 298.216 | Kalinowska, Jedlinska, et al., 1980 | T = 185 to 300 K. Unsmoothed experimental datum.; DH |
147.9 | 303.4 | Griigo'ev, Yanin, et al., 1979 | T = 303 to 463 K. p = 0.98 bar.; DH |
143.77 | 298.15 | Vesely, Zabransky, et al., 1979 | DH |
149.0 | 298.15 | Murthy and Subrahmanyam, 1977 | DH |
143.78 | 298.15 | Vesely, Svoboda, et al., 1977 | DH |
143.87 | 298.15 | Fortier, Benson, et al., 1976 | DH |
144.062 | 298.15 | Fortier and Benson, 1976 | DH |
158.6 | 313.2 | Paz Andrade, Paz, et al., 1970 | DH |
143.8 | 298.15 | Counsell, Lees, et al., 1968 | T = 11 to 350 K.; DH |
146.1 | 298. | Recko, 1968 | T = 24 to 40°C, equation only.; DH |
155.6 | 320. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 21 to 74°C.; DH |
140.21 | 303. | Eucken and Eigen, 1951 | T = 303 to 393 K.; DH |
145.6 | 298.1 | Zhdanov, 1941 | T = 5 to 46°C.; DH |
164.8 | 301.2 | Phillip, 1939 | DH |
136.0 | 270. | Mitsukuri and Hara, 1929 | T = 170 to 270 K.; DH |
192.9 | 298.1 | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 43.5 J/mol*K. Revision of previous data.; DH |
133.5 | 275.4 | Parks and Huffman, 1927 | T = 86 to 275 K. Value is unsmoothed experimental datum.; DH |
133.5 | 275.0 | Parks and Huffman, 1926 | T = 86 to 275 K. Value is unsmoothed experimental datum.; DH |
131.3 | 274.6 | Gibson, Parks, et al., 1920 | T = 77 to 274.6 K. Unsmoothed experimental datum.; DH |
144.8 | 298. | von Reis, 1881 | T = 289 to 363 K.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
106.3 | 150. | Counsell, Lees, et al., 1968 | glass phase; T = 10 to 150 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 | 370.3 ± 0.5 | K | AVG | N/A | Average of 127 out of 139 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 146.7 | K | N/A | Tschamler, Richter, et al., 1949 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 147. | K | N/A | Timmermans, 1935 | Uncertainty assigned by TRC = 3. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 148.75 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 148.75 | K | N/A | Counsell, Lees, et al., 1968, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 147.0 | K | N/A | Parks and Huffman, 1926, 2 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 536.9 ± 0.8 | K | AVG | N/A | Average of 20 out of 25 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 52. ± 1. | bar | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.218 | l/mol | N/A | Gude and Teja, 1995 | |
Vc | 0.216 | l/mol | N/A | Zawisza and Vejrosta, 1982 | Uncertainty assigned by TRC = 0.001 l/mol; Visual; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.58 ± 0.06 | mol/l | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 47. ± 1. | kJ/mol | AVG | N/A | Average of 15 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
41.44 | 370.3 | N/A | Majer and Svoboda, 1985 | |
41.2 | 371. | N/A | Wormald and Vine, 2000 | AC |
35.2 | 423. | N/A | Wormald and Vine, 2000 | AC |
29.4 | 453. | N/A | Wormald and Vine, 2000 | AC |
21.0 | 498. | N/A | Wormald and Vine, 2000 | AC |
11.4 | 528. | N/A | Wormald and Vine, 2000 | AC |
47.0 | 318. | N/A | Aucejo, Gonzalez-Alfaro, et al., 1995 | Based on data from 303. to 370. K.; AC |
42.9 | 375. | N/A | Ortega, Susial, et al., 1990 | Based on data from 360. to 377. K.; AC |
48.0 | 214. | A | Stephenson and Malanowski, 1987 | Based on data from 200. to 228. K.; AC |
43.5 | 366. | A | Stephenson and Malanowski, 1987 | Based on data from 356. to 376. K.; AC |
42.3 | 384. | A | Stephenson and Malanowski, 1987 | Based on data from 369. to 407. K.; AC |
40.1 | 416. | A | Stephenson and Malanowski, 1987 | Based on data from 401. to 482. K.; AC |
36.5 | 492. | A | Stephenson and Malanowski, 1987 | Based on data from 478. to 507. K.; AC |
46.4 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
45.7 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
44.9 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
44.0 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
43.2 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
42.4 ± 0.1 | 363. | C | Svoboda, Veselý, et al., 1973 | AC |
49.3 | 290. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 275. to 373. K.; AC |
44.7 | 348. | EB | Ambrose, Counsell, et al., 1970 | Based on data from 333. to 377. K. See also Stephenson and Malanowski, 1987.; AC |
46.9 | 307. | DTA | Kemme and Kreps, 1969 | Based on data from 292. to 370. K.; AC |
46.7 | 303. | N/A | Van Ness, Soczek, et al., 1967 | Based on data from 288. to 348. K.; AC |
40.7 | 420. | N/A | Ambrose and Townsend, 1963 | Based on data from 405. to 537. K.; AC |
44.3 | 353. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 338. to 378. K.; AC |
44.1 | 358. | N/A | Mathews and McKetta, 1961 | Based on data from 343. to 385. K.; AC |
43.9 ± 0.1 | 343. | C | Mathews and McKetta, 1961 | AC |
42.3 ± 0.1 | 360. | C | Mathews and McKetta, 1961 | AC |
41.2 ± 0.1 | 370. | C | Mathews and McKetta, 1961 | AC |
40.3 ± 0.1 | 378. | C | Mathews and McKetta, 1961 | AC |
39.7 ± 0.1 | 384. | C | Mathews and McKetta, 1961 | AC |
45.5 | 321. to 367. | N/A | Aronovich, Kastorskii, et al., 1959 | AC |
43.2 | 354. | N/A | Williamson and Harrison, 1957 | AC |
44.99 ± 0.42 | 333.13 | V | Williamson and Harrison, 1957, 2 | ALS |
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 390. |
---|---|
A (kJ/mol) | 52.06 |
α | -0.8386 |
β | 0.6888 |
Tc (K) | 536.7 |
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 |
---|---|---|---|---|---|
333.32 to 377.72 | 4.87601 | 1441.629 | -74.299 | Ambrose and Sprake, 1970 | Coefficents calculated by NIST from author's data. |
292.4 to 370.5 | 5.31384 | 1690.864 | -51.804 | Kemme and Kreps, 1969 | |
405.46 to 536.71 | 4.59871 | 1300.491 | -86.364 | Ambrose and Townsend, 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
5.372 | 148.75 | Counsell, Lees, et al., 1968 | DH |
5.4 | 148.7 | van Miltenburg and van den Berg, 2004 | AC |
5.37 | 148.8 | Counsell, Lees, et al., 1968, 2 | AC |
5.192 | 147.0 | Parks and Huffman, 1926 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.11 | 148.75 | Counsell, Lees, et al., 1968 | DH |
35.3 | 147.0 | Parks and Huffman, 1926 | 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: C3H9O+ + C3H8O = (C3H9O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 127. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; switching reaction(CH3CNH+)CH3CN; Lias, Liebman, et al., 1984, Deakyne, Meot-Ner (Mautner), et al., 1986; M |
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, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 112. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; switching reaction(CH3CNH+)CH3CN; Lias, Liebman, et al., 1984, Deakyne, Meot-Ner (Mautner), et al., 1986; M |
ΔrS° | 126. | 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° | 94.6 | 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 |
By formula: C2H7O+ + C3H8O = (C2H7O+ • C3H8O)
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° | 119. | 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° | 91.2 | 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: C4H11O+ + C3H8O = (C4H11O+ • C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 133. | 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° | 122. | 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° | 96.2 | 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 |
C3H7O- + =
By formula: C3H7O- + H+ = C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1572. ± 5.4 | kJ/mol | D-EA | Ellison, Engleking, et al., 1982 | gas phase; B |
ΔrH° | 1573. ± 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° | 1574. ± 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° | 1545. ± 5.9 | kJ/mol | H-TS | Ellison, Engleking, et al., 1982 | gas phase; B |
ΔrG° | 1546. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1546. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
By formula: C4H9O- + C3H8O = (C4H9O- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 114. ± 12. | kJ/mol | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | J/mol*K | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 77.8 ± 8.4 | kJ/mol | IMRE | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
By formula: C8H5- + C3H8O = (C8H5- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 94. ± 12. | kJ/mol | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | J/mol*K | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 57.7 ± 8.4 | kJ/mol | IMRE | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
By formula: C3H7O- + C3H8O = (C3H7O- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 119. ± 12. | kJ/mol | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | J/mol*K | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 81.2 ± 8.4 | kJ/mol | IMRE | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B,M |
By formula: Cl- + C3H8O = (Cl- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 85.4 ± 2.1 | kJ/mol | TDAs | Hiraoka, 1987 | gas phase; B,B,M |
ΔrH° | 74.1 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 121. | 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° | 48.95 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
ΔrG° | 49.0 ± 8.4 | kJ/mol | TDAs | Hiraoka, 1987 | gas phase; B |
ΔrG° | 45.2 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: C3H5O+ + C3H8O = (C3H5O+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 90.8 | kJ/mol | ICR | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | J/mol*K | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 54.4 | kJ/mol | ICR | Caldwell, Rozeboom, et al., 1984 | gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M |
By formula: C3H9Si+ + C3H8O = (C3H9Si+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 181. | 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 |
---|---|---|---|---|
121. | 468. | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+))H2O, Entropy change calculated or estimated; M |
By formula: C3H9Sn+ + C3H8O = (C3H9Sn+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 149. | 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° | 130. | 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 |
---|---|---|---|---|
78.2 | 525. | PHPMS | Stone and Splinter, 1984 | gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M |
By formula: C5H11O- + C3H8O = (C5H11O- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 113. ± 12. | kJ/mol | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 76.1 ± 8.4 | kJ/mol | IMRE | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B |
By formula: C3H5O- + C3H8O = (C3H5O- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 90. ± 12. | kJ/mol | N/A | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 54.0 ± 8.4 | kJ/mol | IMRE | Caldwell, Rozeboom, et al., 1984 | gas phase; Reanchored to average data from Paul and Kebarle, 1990 and Meot-ner and Sieck, 1986.; value altered from reference due to change in acidity scale; B |
By formula: (C3H9O+ • 7C3H8O) + C3H8O = (C3H9O+ • 8C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | N/A | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
17. | 215. | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
By formula: (Cl- • 7C3H8O) + C3H8O = (Cl- • 8C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.2 ± 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° | 7.5 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; Estimated entropy; single temperature measurement; B |
By formula: F- + C3H8O = (F- • C3H8O)
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° | 106. | 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: (C3H9O+ • 2C3H8O) + C3H8O = (C3H9O+ • 3C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.2 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrH° | 59.4 | kJ/mol | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 107. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrS° | 99.6 | J/mol*K | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
By formula: (C3H9O+ • 3C3H8O) + C3H8O = (C3H9O+ • 4C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 49.8 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrH° | 49.0 | kJ/mol | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 104. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrS° | 96.2 | J/mol*K | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
By formula: (C3H9O+ • C3H8O) + C3H8O = (C3H9O+ • 2C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 90.4 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrH° | 79.1 | kJ/mol | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 131. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrS° | 96.2 | J/mol*K | PHPMS | Hiraoka, Morise, et al., 1986 | gas phase; M |
By formula: C3H6O + H2 = C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -84.3 ± 0.4 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | liquid phase; solvent: Triglyme; Heat of hydrogenation; ALS |
ΔrH° | -69.55 ± 0.76 | kJ/mol | Eqk | Connett, 1972 | gas phase; At 473-524 K; ALS |
ΔrH° | -65.77 ± 0.67 | kJ/mol | Chyd | Buckley and Cox, 1967 | gas phase; ALS |
By formula: (Cl- • 2C3H8O) + C3H8O = (Cl- • 3C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 59.4 ± 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° | 20. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (Cl- • 3C3H8O) + C3H8O = (Cl- • 4C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 55.6 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 134. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 15. ± 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° | 52.7 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 138. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 11. ± 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° | 48.5 ± 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° | 9.6 ± 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° | 46.0 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 126. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 7.9 ± 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° | 66.1 ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 106. | J/mol*K | PHPMS | Hiraoka and Mizuse, 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 34. ± 4.2 | kJ/mol | TDAs | Hiraoka and Mizuse, 1987 | gas phase; B |
By formula: (C3H9O+ • 4C3H8O) + C3H8O = (C3H9O+ • 5C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.6 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 106. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: (C3H9O+ • 5C3H8O) + C3H8O = (C3H9O+ • 6C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.4 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: (C3H9O+ • 6C3H8O) + C3H8O = (C3H9O+ • 7C3H8O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.6 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 128. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: CH6N+ + C3H8O = (CH6N+ • C3H8O)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 92.0 | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 107. | J/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
By formula: Na+ + C3H8O = (Na+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 108. ± 4.2 | kJ/mol | CIDT | Armentrout and Rodgers, 2000 | RCD |
ΔrH° | 108. ± 4.2 | kJ/mol | CIDT | Rodgers and Armentrout, 1999 | RCD |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
0.0 | 0. | CIDT | Rodgers and Armentrout, 1999 | RCD |
By formula: C3H6O + H2 = C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -130.6 ± 1.8 | kJ/mol | Chyd | Dolliver, Gresham, et al., 1938 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -132. ± 1. kJ/mol; At 355°K; ALS |
By formula: C6H5S- + C3H8O = (C6H5S- • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 62.8 | kJ/mol | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 109. | J/mol*K | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
+ = 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: C10H12O5 + H2O = C7H6O5 + C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -15.4 ± 6.6 | kJ/mol | Eqk | Tewari, Schantz, et al., 1996 | liquid phase; solvent: Toluene; ALS |
+ = C5H8Cl2F2O
By formula: C3H8O + C2Cl2F2 = C5H8Cl2F2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -164. ± 2. | kJ/mol | Cm | Kennedy, Lacher, et al., 1969 | gas phase; ALS |
By formula: C3H8O + HNO3 = C3H7NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -21.8 | kJ/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
By formula: C2H2O + C3H8O = C5H10O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -147.8 | kJ/mol | Cm | Rice and Greenberg, 1934 | gas phase; ALS |
By formula: Li+ + C3H8O = (Li+ • C3H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 171. ± 7.9 | kJ/mol | CIDT | Rodgers and Armentrout, 2000 | RCD |
By formula: C4H2O3 + C3H8O = propyl hydrogen maleate
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -35. | kJ/mol | Kin | Tribunescu, Poraicu, et al., 1978 | liquid phase; ALS |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
110. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
130. | 7500. | M | N/A | |
150. | C | N/A | ||
160. | M | N/A | ||
140. | 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.
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]
Buckley E., 1967
Buckley E.,
Chemical equilibria. Part 2. Dehydrogenation of propanol and butanol,
Trans. Faraday Soc., 1967, 63, 895-901. [all data]
Counsell J.F., 1968
Counsell J.F.,
Thermodynamic properties of organic oxygen compounds. Part XIX. Low-temperature heat capacity and entropy of propan-1-ol, 2-methylpropan-1-ol, and pentan-1-ol,
J. Chem. Soc. A, 1968, 1819-1823. [all data]
Green J.H.S., 1961
Green J.H.S.,
Thermodynamic properties of the normal alcohols C1-C12,
J. Appl. Chem., 1961, 11, 397-404. [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]
Wilhoit R.C., 1973
Wilhoit R.C.,
Physical and thermodynamic properties of aliphatic alcohols,
J. Phys. Chem. Ref. Data, 1973, 2, Suppl. 1, 1-420. [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]
Mathews J.F., 1961
Mathews J.F.,
The thermodynamic properties of the n-propyl alcohol,
J. Phys. Chem., 1961, 65, 758-762. [all data]
Chao J., 1986, 2
Chao J.,
Ideal gas thermodynamic properties of simple alkanols,
Int. J. Thermophys., 1986, 7, 431-442. [all data]
Kobe K.A., 1951
Kobe K.A.,
Thermochemistry for the petrochemical industry. Part XVII. Some C3 oxygenated hydrocarbons,
Petrol. Refiner, 1951, 30 (8), 119-122. [all data]
Zhuravlev E.Z., 1959
Zhuravlev E.Z.,
Isotopic effect on thermodynamic functions of some organic deuterocompounds in the ideal gas state,
Tr. Khim. i Khim. Tekhnol., 1959, 2, 475-485. [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]
Mosselman and Dekker, 1975
Mosselman, C.; Dekker, H.,
Enthalpies of formation of n-alkan-1-ols,
J. Chem. Soc. Faraday Trans. 1, 1975, 417-424. [all data]
Connett, 1972
Connett, J.E.,
Chemical equilibria. 5. Measurement of equilibrium constants for the dehydrogenation of propanol by a vapour flow technique,
J. Chem. Thermodyn., 1972, 4, 233-237. [all data]
Chao and Rossini, 1965
Chao, J.; Rossini, F.D.,
Heats of combustion, formation, and isomerization of nineteen alkanols,
J. Chem. Eng. Data, 1965, 10, 374-379. [all data]
Rossini, 1934
Rossini, F.D.,
Heats of combustion and of formation of the normal aliphatic alcohols in the gaseous and liquid states, and the energies of their atomic linkages,
J. Res. NBS, 1934, 13, 189-197. [all data]
Snelson and Skinner, 1961
Snelson, A.; Skinner, H.A.,
Heats of combustion: sec-propanol, 1,4-dioxan, 1,3-dioxan and tetrahydropyran,
Trans. Faraday Soc., 1961, 57, 2125-2131. [all data]
Green, 1960
Green, J.H.S.,
Revision of the values of the heats of formation of normal alcohols,
Chem. Ind. (London), 1960, 1215-1216. [all data]
Richards and Davis, 1920
Richards, T.W.; Davis, H.S.,
The heats of combustion of benzene, toluene, aliphatic alcohols, cyclohexanol, and other carbon compounds,
J. Am. Chem. Soc., 1920, 42, 1599-1617. [all data]
Counsell, Lees, et al., 1968
Counsell, J.F.; Lees, E.B.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part XIX. Low temperature heat capacity and entropy of propan-1-ol, 2-methyl-propan-1-ol,
and pentan-1-ol, 1968, J. [all data]
Parks and Huffman, 1926
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds. IV. The heat capacities, entropies and free energies of normal propyl alcohol, ethyl ether and dulcitol,
J. Am. Chem. Soc., 1926, 48, 2788-2793. [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]
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]
Benson and D'Arcy, 1982
Benson, G.C.; D'Arcy, P.J.,
Excess isobaric heat capacities of water - n-alcohol mixtures,
J. Chem. Eng. Data, 1982, 27, 439-442. [all data]
Villamanan, Casanova, et al., 1982
Villamanan, M.A.; Casanova, C.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Thermochemical behavior of mixtures of n-alcohol + aliphatic ether: heat capacities and volumes at 298.15 K,
Thermochim. Acta, 1982, 52, 279-283. [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]
Kalinowska, Jedlinska, et al., 1980
Kalinowska, B.; Jedlinska, J.; Woycicki, W.; Stecki, J.,
Heat capacities of liquids at temperatures between 90 and 300 K and at atmospheric pressure. I. Method and apparatus, and the heat capacities of n-heptane, n-hexane, and n-propanol,
J. Chem. Thermodynam., 1980, 12, 891-896. [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]
Vesely, Zabransky, et al., 1979
Vesely, F.; Zabransky, M.; Svoboda, V.; Pick, J.,
The use of mixing calorimeter for measuring heat capacities of liquids,
Coll. Czech. Chem. Commun., 1979, 44, 3529-3532. [all data]
Murthy and Subrahmanyam, 1977
Murthy, N.M.; Subrahmanyam, S.V.,
Behaviour of excess heat capacity of aqueous non-electrolytes,
Indian J. Pure Appl. Phys., 1977, 15, 485-489. [all data]
Vesely, Svoboda, et al., 1977
Vesely, F.; Svoboda, V.; Pick, J.,
Heat capacities of some organic liquids determined with the mixing calorimeter,
1st Czech. Conf. Calorimetry (Lect. Short Commun.), 1977, C9-1-C9-4. [all data]
Fortier, Benson, et al., 1976
Fortier, J.-L.; Benson, G.C.; Picker, P.,
Heat capacities of some organic liquids determined with the Picker flow calorimeter,
J. Chem. Thermodynam., 1976, 8, 289-299. [all data]
Fortier and Benson, 1976
Fortier, J.-L.; Benson, G.C.,
Excess heat capacities of binary liquid mixtures determined with a Picker flow calorimeter,
J. Chem. Thermodynam., 1976, 8, 411-423. [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]
Recko, 1968
Recko, W.M.,
Excess heat capacity of the binary systems formed by n-propyl alcohol with benzene, mesitylene and cyclohexane,
Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1968, 16, 549-552. [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]
Eucken and Eigen, 1951
Eucken, A.; Eigen, M.,
Untersuchung der Assoziationsstruktur in schwerem Wasser und n-Propanol mit Hilfe thermisch-kalorischer Eigenschaften, insbesondere Messungen der spezifischen Wäarmen,
Z. Elektrochem., 1951, 55, 343-354. [all data]
Zhdanov, 1941
Zhdanov, A.K.,
Specific heats of some liquids and azeotropic mixtures,
Zhur. Obshch. Khim., 1941, 11, 471-482. [all data]
Phillip, 1939
Phillip, N.M.,
Adiabatic and isothermal compressibilities of liquids,
Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]
Mitsukuri and Hara, 1929
Mitsukuri, S.; Hara, K.,
Specific heats of acetone, methyl-, ethyl-, and n-propyl-alcohols at low temperatures,
Bull. Chem. Soc. Japan, 1929, 4, 77-81. [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 and Huffman, 1927
Parks, G.S.; Huffman, H.M.,
Studies on glass. I. The transition between the glassy and liquid states in the case of some simple organic compounds,
J. Phys. Chem., 1927, 31, 1842-1855. [all data]
Gibson, Parks, et al., 1920
Gibson, G.E.; Parks, G.S.; Latimer, W.M.,
Entropy changes at low temperatures. II. Ethyl and propyl alcohols and their equal molal mixture,
J. Am. Chem. Soc., 1920, 42, 1542-1550. [all data]
von Reis, 1881
von Reis, M.A.,
Die specifische Wärme flüssiger organischer Verbindungen und ihre Beziehung zu deren Moleculargewicht,
Ann. Physik [3], 1881, 13, 447-464. [all data]
Tschamler, Richter, et al., 1949
Tschamler, H.; Richter, E.; Wettig, F.,
Mixtures of Primry Aliphatic Alcohols with Chlorex and Other Organic Substances. Binary Liquid Mixtures XII.,
Monatsh. Chem., 1949, 80, 749. [all data]
Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
Bull. Soc. Chim. Belg., 1935, 44, 17-40. [all data]
Wilhoit, Chao, et al., 1985
Wilhoit, R.C.; Chao, J.; Hall, K.R.,
Thermodynamic Properties of Key Organic Compounds in the Carbon Range C1 to C4. Part 1. Properties of Condensed Phases,
J. Phys. Chem. Ref. Data, 1985, 14, 1. [all data]
Counsell, Lees, et al., 1968, 2
Counsell, J.F.; Lees, E.B.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part XIX. Low-temperature heat capacity and entropy of propan-1-ol, 2-methylpropan-1-ol, and pentan-1-ol,
J. Chem. Soc., A, 1968, 1819, https://doi.org/10.1039/j19680001819
. [all data]
Parks and Huffman, 1926, 2
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds: IV the heat capacites, entropies, and free energies of normal propyl alcohol, ethyl ether, and dulcitol,
J. Am. Chem. Soc., 1926, 48, 2788-93. [all data]
Gude and Teja, 1995
Gude, M.; Teja, A.S.,
Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols,
J. Chem. Eng. Data, 1995, 40, 1025-1036. [all data]
Zawisza and Vejrosta, 1982
Zawisza, A.; Vejrosta, J.,
High-pressure liquid-vapor equilibria, critical stat, and p(V, T, x) up to 573.15 K and 5.066 MPa for (heptane + propan-1-ol),
J. Chem. Thermodyn., 1982, 14, 239-49. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Wormald and Vine, 2000
Wormald, C.J.; Vine, M.D.,
Specific enthalpy increments for propan-1-ol at temperatures up to 573.2 K and 11.3 MPa,
The Journal of Chemical Thermodynamics, 2000, 32, 3, 329-339, https://doi.org/10.1006/jcht.1999.0594
. [all data]
Aucejo, Gonzalez-Alfaro, et al., 1995
Aucejo, Antonio; Gonzalez-Alfaro, Vicenta; Monton, Juan B.; Vazquez, M. Isabel,
Isobaric Vapor-Liquid Equilibria of Trichloroethylene with 1-Propanol and 2-Propanol at 20 and 100 kPa,
J. Chem. Eng. Data, 1995, 40, 1, 332-335, https://doi.org/10.1021/je00017a073
. [all data]
Ortega, Susial, et al., 1990
Ortega, Juan; Susial, Pedro; De Alfonso, Casiano,
Isobaric vapor-liquid equilibrium of methyl butanoate with ethanol and 1-propanol binary systems,
J. Chem. Eng. Data, 1990, 35, 2, 216-219, https://doi.org/10.1021/je00060a037
. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2
. [all data]
Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J.,
Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature,
Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539
. [all data]
Wilhoit and Zwolinski, 1973
Wilhoit, R.C.; Zwolinski, B.J.,
Physical and thermodynamic properties of aliphatic alcohols,
J. Phys. Chem. Ref. Data Suppl., 1973, 1, 2, 1. [all data]
Ambrose, Counsell, et al., 1970
Ambrose, D.; Counsell, J.F.; Davenport, A.J.,
The use of Chebyshev polynomials for the representation of vapour pressures between the triple point and the critical point,
The Journal of Chemical Thermodynamics, 1970, 2, 2, 283-294, https://doi.org/10.1016/0021-9614(70)90093-5
. [all data]
Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I.,
Vapor pressure of primary n-alkyl chlorides and alcohols,
J. Chem. Eng. Data, 1969, 14, 1, 98-102, https://doi.org/10.1021/je60040a011
. [all data]
Van Ness, Soczek, et al., 1967
Van Ness, Hendrick C.; Soczek, C.A.; Peloquin, G.L.; Machado, R.L.,
Thermodynamic excess properties of three alcohol-hydrocarbon systems,
J. Chem. Eng. Data, 1967, 12, 2, 217-224, https://doi.org/10.1021/je60033a017
. [all data]
Ambrose and Townsend, 1963
Ambrose, D.; Townsend, R.,
681. Thermodynamic properties of organic oxygen compounds. Part IX. The critical properties and vapour pressures, above five atmospheres, of six aliphatic alcohols,
J. Chem. Soc., 1963, 3614, https://doi.org/10.1039/jr9630003614
. [all data]
Biddiscombe, Collerson, et al., 1963
Biddiscombe, D.P.; Collerson, R.R.; Handley, R.; Herington, E.F.G.; Martin, J.F.; Sprake, C.H.S.,
364. Thermodynamic properties of organic oxygen compounds. Part VIII. Purification and vapour pressures of the propyl and butyl alcohols,
J. Chem. Soc., 1963, 1954, https://doi.org/10.1039/jr9630001954
. [all data]
Mathews and McKetta, 1961
Mathews, J.F.; McKetta, J.J.,
THE THERMODYNAMIC PROPERTIES OF n-PROPYL ALCOHOL,
J. Phys. Chem., 1961, 65, 5, 758-762, https://doi.org/10.1021/j100823a013
. [all data]
Aronovich, Kastorskii, et al., 1959
Aronovich, Kh.A.; Kastorskii, L.P.; Fedorova, K.F.,
Zh. Fiz. Khim., 1959, 41, 20. [all data]
Williamson and Harrison, 1957
Williamson, Kenneth D.; Harrison, Roland H.,
Heats of Vaporization of 1,1,2-Trichloroethane, 1-Propanol, and 2-Propanol; Vapor Heat Capacity of 1,1,2-Trichloroethane,
J. Chem. Phys., 1957, 26, 6, 1409, https://doi.org/10.1063/1.1743555
. [all data]
Williamson and Harrison, 1957, 2
Williamson, K.D.; Harrison, R.H.,
Heats of vaporization of 1,1,2-trichloroethane, 1-propanol, and 2-propanol; vapor heat capacity of 1,1,2-trichloroethane,
J. Chem. Phys., 1957, 26, 1409-14. [all data]
Ambrose and Sprake, 1970
Ambrose, D.; Sprake, C.H.S.,
Thermodynamic properties of organic oxygen compounds XXV. Vapour pressures and normal boiling temperatures of aliphatic alcohols,
The Journal of Chemical Thermodynamics, 1970, 2, 5, 631-645, https://doi.org/10.1016/0021-9614(70)90038-8
. [all data]
Ambrose and Townsend, 1963, 2
Ambrose, D.; Townsend, R.,
Thermodynamic Properties of Organic Oxygen Compounds. Part 9. The Critical Properties and Vapour Pressures, above Five Atmospheres, of Six Aliphatic Alcohols,
J. Chem. Soc., 1963, 3614-3625, https://doi.org/10.1039/jr9630003614
. [all data]
van Miltenburg and van den Berg, 2004
van Miltenburg, J. Cees; van den Berg, Gerrit J.K.,
Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K,
J. Chem. Eng. Data, 2004, 49, 3, 735-739, https://doi.org/10.1021/je0499768
. [all data]
Meot-Ner (Mautner), 1992
Meot-Ner (Mautner), M.,
Intermolecular Forces in Organic Clusters,
J. Am. Chem. Soc., 1992, 114, 9, 3312, https://doi.org/10.1021/ja00035a024
. [all data]
Lias, Liebman, et al., 1984
Lias, S.G.; Liebman, J.F.; Levin, R.D.,
Evaluated gas phase basicities and proton affinities of molecules heats of formation of protonated molecules,
J. Phys. Chem. Ref. Data, 1984, 13, 695. [all data]
Deakyne, Meot-Ner (Mautner), et al., 1986
Deakyne, C.A.; Meot-Ner (Mautner), M.; Campbell, C.L.; Hughes, M.G.; Murphy, S.P.,
Multicomponent Cluster Ions. 1. The Acetonitrile - Water System,
J. Chem. Phys., 1986, 90, 4648. [all data]
Larson and McMahon, 1982
Larson, J.W.; McMahon, T.B.,
Formation, Thermochemistry, and Relative Stabilities of Proton - Bound dimers of Oxygen n - Donor Bases from Ion Cyclotron Resonance Solvent - Exchange Equilibria Measurements,
J. Am. Chem. Soc., 1982, 104, 23, 6255, https://doi.org/10.1021/ja00387a016
. [all data]
Grimsrud and Kebarle, 1973
Grimsrud, E.P.; Kebarle, P.,
Gas Phase Ion Equilibria Studies of the Solvation of the Hydrogen Ion by Methanol, Dimethyl Ether and Water. Effect of Hydrogen Bonding,
J. Am. Chem. Soc., 1973, 95, 24, 7939, https://doi.org/10.1021/ja00805a002
. [all data]
Keesee and Castleman, 1986
Keesee, R.G.; Castleman, A.W., Jr.,
Thermochemical data on Ggs-phase ion-molecule association and clustering reactions,
J. Phys. Chem. Ref. Data, 1986, 15, 1011. [all data]
Ellison, Engleking, et al., 1982
Ellison, G.B.; Engleking, P.C.; Lineberger, W.C.,
Photoelectron spectroscopy of alkoxide and enolate negative ions,
J. Phys. Chem., 1982, 86, 4873. [all data]
Bartmess, Scott, et al., 1979
Bartmess, J.E.; Scott, J.A.; McIver, R.T., Jr.,
The gas phase acidity scale from methanol to phenol,
J. Am. Chem. Soc., 1979, 101, 6047. [all data]
Haas and Harrison, 1993
Haas, M.J.; Harrison, A.G.,
The Fragmentation of Proton-Bound Cluster Ions and the Gas-Phase Acidities of Alcohols,
Int. J. Mass Spectrom. Ion Proc., 1993, 124, 2, 115, https://doi.org/10.1016/0168-1176(93)80003-W
. [all data]
Caldwell, Rozeboom, et al., 1984
Caldwell, G.; Rozeboom, M.D.; Kiplinger, J.P.; Bartmess, J.E.,
Anion-alcohol hydrogen bond strengths in the gas phase,
J. Am. Chem. Soc., 1984, 106, 4660. [all data]
Paul and Kebarle, 1990
Paul, G.J.C.; Kebarle, P.,
Thermodynamics of the Association Reactions OH- - H2O = HOHOH- and CH3O- - CH3OH = CH3OHOCH3- in the Gas Phase,
J. Phys. Chem., 1990, 94, 12, 5184, https://doi.org/10.1021/j100375a076
. [all data]
Meot-ner and Sieck, 1986
Meot-ner, M.; Sieck, L.W.,
Relative acidities of water and methanol, and the stabilities of the dimer adducts,
J. Phys. Chem., 1986, 90, 6687. [all data]
Meot-Ner(Mautner), 1986
Meot-Ner(Mautner), M.,
Comparative Stabilities of Cationic and Anionic Hydrogen-Bonded Networks. Mixed Clusters of Water-Methanol,
J. Am. Chem. Soc., 1986, 108, 20, 6189, https://doi.org/10.1021/ja00280a014
. [all data]
Hiraoka, 1987
Hiraoka, K.,
Relation Between Gas Phase Stepwise and Bulk Solvation of Cl- with Water and Aliphatic Alcohols,
Bull. Chem. Soc. Japan, 1987, 60, 7, 2555, https://doi.org/10.1246/bcsj.60.2555
. [all data]
Larson and McMahon, 1984
Larson, J.W.; McMahon, T.B.,
Hydrogen bonding in gas phase anions. An experimental investigation of the interaction between chloride ion and bronsted acids from ICR chloride exchange equilibria,
J. Am. Chem. Soc., 1984, 106, 517. [all data]
Hiraoka and Mizuse, 1987
Hiraoka, K.; Mizuse, S.,
Gas-Phase Solvation of Cl- with H2O, CH3OH, C2H4OH, i-C3H7OH, n-C3H7OH, and t-C4H9OH,
Chem. Phys., 1987, 118, 3, 457, https://doi.org/10.1016/0301-0104(87)85078-4
. [all data]
Larson and McMahon, 1984, 2
Larson, J.W.; McMahon, T.B.,
Gas phase negative ion chemistry of alkylchloroformates,
Can. J. Chem., 1984, 62, 675. [all data]
Wojtyniak and Stone, 1986
Wojtyniak, A.C.M.; Stone, A.J.,
A High-Pressure Mass Spectrometric Study of the Bonding of Trimethylsilylium to Oxygen and Aromatic Bases,
Can. J. Chem., 1986, 74, 59. [all data]
Stone and Splinter, 1984
Stone, J.A.; Splinter, D.E.,
A high-pressure mass spectrometric study of the binding of (CH3)3Sn+ to lewis bases in the gas phase,
Int. J. Mass Spectrom. Ion Processes, 1984, 59, 169. [all data]
Larson and McMahon, 1983
Larson, J.W.; McMahon, T.B.,
Strong hydrogen bonding in gas-phase anions. An ion cyclotron resonance determination of fluoride binding energetics to bronsted acids from gas-phase fluoride exchange equilibria measurements,
J. Am. Chem. Soc., 1983, 105, 2944. [all data]
Arshadi, Yamdagni, et al., 1970
Arshadi, M.; Yamdagni, R.; Kebarle, P.,
Hydration of Halide Negative Ions in the Gas Phase. II. Comparison of Hydration Energies for the Alkali Positive and Halide Negative Ions,
J. Phys. Chem., 1970, 74, 7, 1475, https://doi.org/10.1021/j100702a014
. [all data]
Hiraoka, Morise, et al., 1986
Hiraoka, K.; Morise, K.; Nishijima, T.; Nakamura, S.; Nakazato, M.; Ohkuma, K.,
Gas Phase Ion Equilibria Studies of Protons and Chloride Ions in Propanol and Acetone,
Int. J. Mass Spectrom. Ion Proc., 1986, 68, 1-2, 99, https://doi.org/10.1016/0168-1176(86)87071-9
. [all data]
Wiberg, Crocker, et al., 1991
Wiberg, K.B.; Crocker, L.S.; Morgan, K.M.,
Thermochemical studies of carbonyl compounds. 5. Enthalpies of reduction of carbonyl groups,
J. Am. Chem. Soc., 1991, 113, 3447-3450. [all data]
Buckley and Cox, 1967
Buckley, E.; Cox, J.D.,
Chemical equilibria. Part 2.-Dehydrogenation of propanol and butanol,
Trans. Faraday Soc., 1967, 63, 895-901. [all data]
Meot-Ner, 1984
Meot-Ner, (Mautner)M.,
The Ionic Hydrogen Bond and Ion Solvation. 1. -NH+ O-, -NH+ N- and -OH+ O- Bonds. Correlations with Proton Affinity. Deviations Due to Structural Effects,
J. Am. Chem. Soc., 1984, 106, 5, 1257, https://doi.org/10.1021/ja00317a015
. [all data]
Armentrout and Rodgers, 2000
Armentrout, P.B.; Rodgers, M.T.,
An Absolute Sodium Cation Affinity Scale: Threshold Collision-Induced Dissociation Experiments and ab Initio Theory,
J. Phys. Chem A, 2000, 104, 11, 2238, https://doi.org/10.1021/jp991716n
. [all data]
Rodgers and Armentrout, 1999
Rodgers, M.T.; Armentrout, P.B.,
Absolute Binding Energies of Sodium Ions to Short-Chain Alcohols, CnH2n+2O, n=1-4, Determined by Threshold Collision-Induced Dissociation Experiments and Ab Initio Theory, 1999, 4955. [all data]
Dolliver, Gresham, et al., 1938
Dolliver, M.A.; Gresham, T.L.; Kistiakowsky, G.B.; Smith, E.A.; Vaughan, W.E.,
Heats of organic reactions. VI. Heats of hydrogenation of some oxygen-containing compounds,
J. Am. Chem. Soc., 1938, 60, 440-450. [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]
Sieck and Meot-ner, 1989
Sieck, L.W.; Meot-ner, M.,
Ionic Hydrogen Bond and Ion Solvation. 8. RS-..HOR Bond Strengths. Correlation with Acidities.,
J. Phys. Chem., 1989, 93, 4, 1586, https://doi.org/10.1021/j100341a079
. [all data]
Wilkinson, Szulejko, et al., 1992
Wilkinson, F.E.; Szulejko, J.E.; Allison, C.E.; Mcmahon, T.B.,
Fourier Transform Ion Cyclotron Resonance Investigation of the Deuterium Isotope Effect on Gas Phase Ion/Molecule Hydrogen Bonding Interactions in Alcohol-Fluoride Adduct Ions,
Int. J. Mass Spectrom., 1992, 117, 487-505, https://doi.org/10.1016/0168-1176(92)80110-M
. [all data]
Operti, Tews, et al., 1988
Operti, L.; Tews, E.C.; Freiser, B.S.,
Determination of Gas-Phase Ligand Binding Energies to Mg+ by FTMS Techniques,
J. Am. Chem. Soc., 1988, 110, 12, 3847, https://doi.org/10.1021/ja00220a020
. [all data]
Tewari, Schantz, et al., 1996
Tewari, Y.B.; Schantz, M.M.; Rekharsky, M.V.; Goldberg, R.N.,
Thermodynamics of the hydrolysis of 3,4,5-trihydroxybenzoic acid propyl ester (n-propylgallate) to 3,4,5-trihydroxybenzoic acid (gallic acid) and propan-1-ol in aqueous media and in toluene,
J. Chem. Thermodyn., 1996, 28, 171-185. [all data]
Kennedy, Lacher, et al., 1969
Kennedy, M.B.; Lacher, J.R.; Park, J.D.,
Reaction heats of organic compounds. VI. Heats of addition of some alcohols to 1,1-dichloro-2,2-difluoroethylene,
Trans. Faraday Soc., 1969, 65, 1435-1442. [all data]
Rubtsov, 1986
Rubtsov, Yu.I.,
Thermodynamic calculation of equilibrium in nitration of alcohols,
Bull. Acad. Sci. USSR, Div. Chem. Sci., 1986, 19-22. [all data]
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]
Tribunescu, Poraicu, et al., 1978
Tribunescu, P.; Poraicu, M.; Merca, E.; Facsko, O.,
Kinetics of mono-N-propylmaleate synthesis,
Bull. Stiint. Teh. Inst. Politeh. "Traian Vuia" Timisoara, Ser. Chim., 1978, 23, 147-151. [all data]
Butler, Ramchandani, et al., 1935
Butler, J.A.V.; Ramchandani, C.N.; Thomson, D.W.,
The Solubility of Non-Electrolytes. Part 1. The Free Energy of Hydration of Some Alphatic Alcohols,
J. Chem. Soc., 1935, 280-285, https://doi.org/10.1039/jr9350000280
. [all data]
Butler, Thomson, et al., 1933
Butler, J.A.V.; Thomson, D.W.; Maclennan, W.H.,
The Free Energy of the Normal Aliphatic Alcohols in Aqueous Solution. Part I. The Partial Vapor Pressures of Aqueous Solutions of Methyl, n-Propyl, and n-Butyl Alcohols. Part II. THe Solubilities of,
J. Chem. Soc., 1933, 1933, 674-686. [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 Cp,solid Constant pressure heat capacity of solid Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions S°solid,1 bar Entropy of solid at standard conditions (1 bar) 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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