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, Phase change data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled 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 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 355.5 ± 0.4 | K | AVG | N/A | Average of 102 out of 118 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 185.75 | K | N/A | Ogimachi, Corcoran, et al., 1961 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 185.35 | K | N/A | Anonymous, 1958 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 184.9 ± 0.6 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 509. ± 2. | K | AVG | N/A | Average of 19 out of 20 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 49. ± 5. | bar | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.222 | l/mol | N/A | Gude and Teja, 1995 | |
Vc | 0.223 | l/mol | N/A | Ambrose, Counsell, et al., 1978 | Uncertainty assigned by TRC = 0.003 l/mol; PVT compatible with values chosen.; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.51 ± 0.02 | mol/l | N/A | Gude and Teja, 1995 | |
ρc | 4.54 | mol/l | N/A | Teja, Lee, et al., 1989 | TRC |
ρc | 4.538 | mol/l | N/A | Ambrose and Townsend, 1963 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 45. ± 3. | kJ/mol | AVG | N/A | Average of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
39.85 | 355.4 | N/A | Majer and Svoboda, 1985 | |
43.2 | 337. | N/A | Segura, Galindo, et al., 2002 | Based on data from 322. to 355. K.; AC |
39.8 | 355. | N/A | Wormald and Vine, 2000 | AC |
29.7 | 423. | N/A | Wormald and Vine, 2000 | AC |
23.7 | 453. | N/A | Wormald and Vine, 2000 | AC |
16.5 | 483. | N/A | Wormald and Vine, 2000 | AC |
10.5 | 503. | N/A | Wormald and Vine, 2000 | AC |
44.8 | 315. | N/A | Aucejo, Gonzalez-Alfaro, et al., 1995 | Based on data from 300. to 355. K.; AC |
50.3 | 213. | A | Stephenson and Malanowski, 1987 | Based on data from 195. to 228. K.; AC |
42.0 | 355. | A | Stephenson and Malanowski, 1987 | Based on data from 347. to 368. K.; AC |
41.3 | 365. | A | Stephenson and Malanowski, 1987 | Based on data from 350. to 383. K.; AC |
39.2 | 394. | A | Stephenson and Malanowski, 1987 | Based on data from 379. to 461. K.; AC |
35.3 | 468. | A | Stephenson and Malanowski, 1987 | Based on data from 453. to 508. K.; AC |
43.1 | 340. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 325. to 362. K. See also Ambrose, Counsell, et al., 1970.; AC |
45.7 | 288. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 273. to 374. K.; AC |
45.5 | 303. | N/A | Van Ness, Soczek, et al., 1967 | Based on data from 288. to 348. K.; AC |
42.7 ± 0.1 | 330. | C | Berman, Larkam, et al., 1964 | AC |
41.0 ± 0.1 | 346. | C | Berman, Larkam, et al., 1964 | AC |
39.8 ± 0.1 | 355. | C | Berman, Larkam, et al., 1964 | AC |
38.9 ± 0.1 | 363. | C | Berman, Larkam, et al., 1964 | AC |
39.1 | 410. | N/A | Ambrose and Townsend, 1963, 2 | Based on data from 395. to 508. K.; AC |
42.8 | 344. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 329. to 363. K.; AC |
43.2 | 324. | C | Hales, Cox, et al., 1963 | AC |
41.7 | 339. | C | Hales, Cox, et al., 1963 | AC |
39.8 | 355. | C | Hales, Cox, et al., 1963 | AC |
43.40 ± 0.08 | 324.11 | V | Williamson and Harrison, 1957 | ALS |
41.1 | 369. | N/A | Foz Gazulla, Morcilio, et al., 1955 | Based on data from 354. to 420. K.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 298. to 380. |
---|---|
A (kJ/mol) | 53.38 |
α | -0.708 |
β | 0.6538 |
Tc (K) | 508.3 |
Reference | Majer and Svoboda, 1985 |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
395.1 to 508.24 | 4.57795 | 1221.423 | -87.474 | Ambrose and Townsend, 1963, 3 | Coefficents calculated by NIST from author's data. |
329.92 to 362.41 | 4.8610 | 1357.427 | -75.814 | Biddiscombe, Collerson, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
5.410 | 185.20 | Andon, Counsell, et al., 1963 | DH |
5.372 | 184.67 | Kelley, 1929 | DH |
5.41 | 185.2 | Domalski and Hearing, 1996 | AC |
5.301 | 184.6 | Parks and Kelley, 1928 | DH |
5.297 | 184.6 | Parks and Kelley, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
29.21 | 185.20 | Andon, Counsell, et al., 1963 | DH |
29.09 | 184.67 | Kelley, 1929 | DH |
28.72 | 184.6 | Parks and Kelley, 1928 | DH |
28.7 | 184.6 | Parks and Kelley, 1925 | DH |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Phase change data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C3H8O+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 10.17 ± 0.02 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 793.0 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 762.6 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
796. ± 6. | Cao and Holmes, 2001 | MM |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.15 ± 0.07 | EI | Bowen and Maccoll, 1984 | LBLHLM |
10.10 ± 0.02 | PI | Potapov and Sorokin, 1972 | LLK |
10.29 ± 0.02 | PE | Cocksey, Eland, et al., 1971 | LLK |
10.18 | PE | Dewar and Worley, 1969 | RDSH |
10.12 ± 0.03 | PI | Refaey and Chupka, 1968 | RDSH |
10.15 ± 0.05 | PI | Watanabe, 1957 | RDSH |
10.44 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
10.49 ± 0.03 | PE | Peel and Willett, 1975 | Vertical value; LLK |
10.42 | PE | Robin and Kuebler, 1973 | Vertical value; LLK |
10.36 | PE | Katsumata, Iwai, et al., 1973 | Vertical value; LLK |
10.42 | PE | Baker, Betteridge, et al., 1971 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH3+ | 30.2 ± 0.2 | ? | EI | Olmsted, Street, et al., 1964 | RDSH |
CH3O+ | 12.5 | ? | EI | Friedman, Long, et al., 1957 | RDSH |
C2H3+ | 14.6 | ? | EI | Friedman, Long, et al., 1957 | RDSH |
C2H4O+ | 10.27 ± 0.09 | CH4 | EI | Bowen and Maccoll, 1984 | LBLHLM |
C2H4O+ | 10.26 | CH4 | EI | Holmes, Burgers, et al., 1982 | LBLHLM |
C2H4O+ | 10.23 ± 0.02 | CH4 | PI | Potapov and Sorokin, 1972 | LLK |
C2H4O+ | 10.27 ± 0.03 | CH4 | PI | Refaey and Chupka, 1968 | RDSH |
C2H5O+ | 10.20 ± 0.08 | CH3 | EI | Bowen and Maccoll, 1984 | LBLHLM |
C2H5O+ | 10.26 | CH3 | EI | Lossing, 1977 | LLK |
C2H5O+ | 10.40 ± 0.03 | CH3 | PI | Potapov and Sorokin, 1972 | LLK |
C2H5O+ | 10.70 | CH3 | EI | Haney and Franklin, 1969 | RDSH |
C2H5O+ | 10.40 | CH3 | PI | Refaey and Chupka, 1968 | RDSH |
C3H6+ | ~12.0 ± 0.9 | H2O | EI | Bowen and Maccoll, 1984 | LBLHLM |
C3H6+ | ~12.0 | H2O | PI | Refaey and Chupka, 1968 | RDSH |
C3H7+ | 11.6 | OH | PI | Refaey and Chupka, 1968 | RDSH |
C3H7O+ | ≤10.48 ± 0.08 | H | EI | Bowen and Maccoll, 1984 | LBLHLM |
C3H7O+ | ≤10.48 | H | EI | Lossing, 1977 | LLK |
C3H7O+ | 10.3 ± 0.5 | H | PI | Potapov and Sorokin, 1972 | LLK |
C3H7O+ | 10.6 | H | PI | Refaey and Chupka, 1968 | RDSH |
C3H7O+ | 11.85 | H | EI | Lambdin, Tuffly, et al., 1959 | RDSH |
De-protonation 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 |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Buckley and Herington, 1965
Buckley, E.; Herington, E.F.G.,
Equilibria in some secondary alcohol + hydrogen + ketone systems,
Trans. Faraday Soc., 1965, 61, 1618-1625. [all data]
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]
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]
Parks, Mosley, et al., 1950
Parks, G.S.; Mosley, J.R.; Peterson, P.V., Jr.,
Heats of combustion and formation of some organic compounds containing oxygen,
J. Chem. Phys., 1950, 18, 152. [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]
Green J.H.S., 1963
Green J.H.S.,
Thermodynamic properties of organic oxygen compounds. Part 12. Vibrational assignment and calculated thermodynamic properties 0-1000 K of isopropyl alcohol,
Trans. Faraday Soc., 1963, 59, 1559-1563. [all data]
Chao J., 1986
Chao J.,
Ideal gas thermodynamic properties of simple alkanols,
Int. J. Thermophys., 1986, 7, 431-442. [all data]
Chao J., 1986, 2
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]
Stromsoe E., 1970
Stromsoe E.,
Heat capacity of alcohol vapors at atmospheric pressure,
J. Chem. Eng. Data, 1970, 15, 286-290. [all data]
Parks G.S., 1940
Parks G.S.,
Some heat capacity data for isopropyl alcohol vapor,
J. Chem. Phys., 1940, 8, 429. [all data]
Hales J.L., 1963
Hales J.L.,
Thermodynamic properties of organic oxygen compounds. Part 10. Measurement of vapor heat capacities and latent heats of vaporization of isopropyl alcohol,
Trans. Faraday Soc., 1963, 59, 1544-1554. [all data]
Berman N.S., 1964
Berman N.S.,
Vapor heat capacity and heat of vaporization of 2-propanol,
J. Chem. Eng. Data, 1964, 9, 218-219. [all data]
Ogimachi, Corcoran, et al., 1961
Ogimachi, N.N.; Corcoran, J.M.; Kruse. H.W.,
Thermal Analysis of Systems of Hydrazine with Propyl Alcohol, Isopropyl Alcohol, and Allyl Alcohol,
J. Chem. Eng. Data, 1961, 6, 238. [all data]
Anonymous, 1958
Anonymous, X.,
Am. Pet. Inst. Res. Proj. 50, 1958, Unpublished, 1958. [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]
Ambrose, Counsell, et al., 1978
Ambrose, D.; Counsell, J.F.; Lawrenson, I.J.; Lewis, G.B.,
Thermodynamic properties of organic oxygen compounds XLVII. Pressure, volume, temperature relations and thermodynamic properties of propan-2-ol,
J. Chem. Thermodyn., 1978, 10, 1033-1043. [all data]
Teja, Lee, et al., 1989
Teja, A.S.; Lee, R.J.; Rosenthal, D.J.; Anselme, M.J.,
Correlation of the Critical Properties of Alkanes and Alkanols
in 5th IUPAC Conference on Alkanes and AlkanolsGradisca, 1989. [all data]
Ambrose and Townsend, 1963
Ambrose, D.; Townsend, R.,
Thermodynamic Properties of Organic Oxygen Compounds IX. The Critical Properties and Vapor Pressures Above Five Atmospheres of Six Aliphatic Alcohols,
J. Chem. Soc., 1963, 54, 3614-25. [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]
Segura, Galindo, et al., 2002
Segura, Hugo; Galindo, Graciela; Reich, Ricardo; Wisniak, Jaime; Loras, Sonia,
Isobaric Vapor-Liquid Equilibria and Densities for the System Methyl 1,1-Dimethylethyl Ether +2-Propanol,
Physics and Chemistry of Liquids, 2002, 40, 3, 277-294, https://doi.org/10.1080/0031910021000004865
. [all data]
Wormald and Vine, 2000
Wormald, C.J.; Vine, M.D.,
Specific enthalpy increments for propan-2-ol at temperatures up to 563.2 K and pressures up to 11.3 MPa,
The Journal of Chemical Thermodynamics, 2000, 32, 5, 659-669, https://doi.org/10.1006/jcht.1999.0631
. [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]
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]
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]
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]
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]
Berman, Larkam, et al., 1964
Berman, Neil S.; Larkam, Charles W.; McKetta, John J.,
Vapor Heat Capacity and Heat of Vaporization of 2-Propanol.,
J. Chem. Eng. Data, 1964, 9, 2, 218-219, https://doi.org/10.1021/je60021a020
. [all data]
Ambrose and Townsend, 1963, 2
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]
Hales, Cox, et al., 1963
Hales, J.L.; Cox, J.D.; Lees, E.B.,
Thermodynamic properties of organic oxygen compounds. Part 10.-Measurement of vapour heat capacities and latent heats of vaporization of isopropyl alcohol,
Trans. Faraday Soc., 1963, 59, 1544. [all data]
Williamson and Harrison, 1957
Williamson, K.D.; Harrison, R.H.,
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Foz Gazulla, Morcilio, et al., 1955
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Ambrose and Townsend, 1963, 3
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Biddiscombe, Collerson, et al., 1963, 2
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Andon, Counsell, et al., 1963
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Kelley, 1929
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Parks and Kelley, 1928
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Parks and Kelley, 1925
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Hunter and Lias, 1998
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Low energy, low temperature mass spectra,
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Potapov and Sorokin, 1972
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Khim. Vys. Energ., 1972, 6, 387. [all data]
Cocksey, Eland, et al., 1971
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J. Chem. Soc., 1971, (B), 790. [all data]
Dewar and Worley, 1969
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Robin and Kuebler, 1973
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Excited electronic states of the simple alcohols,
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Katsumata, Iwai, et al., 1973
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Baker, Betteridge, et al., 1971
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Friedman, Long, et al., 1957
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Holmes, Burgers, et al., 1982
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Alkane elimination from ionized alkanols,
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Heats of formation of some isomeric [CnH2n+1]+ ions. Substitutional effects on ion stability,
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Lambdin, Tuffly, et al., 1959
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Bartmess, Scott, et al., 1979
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. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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