1-Propanol

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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-61.2 ± 0.7kcal/molAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
S°gas77.077cal/mol*KN/AChao J., 1986Other 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 (cal/mol*K) Temperature (K) Reference Comment
9.69950.Thermodynamics Research Center, 1997p=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
12.32100.
14.08150.
15.86200.
19.17273.15
20.45 ± 0.033298.15
20.54300.
25.820400.
30.638500.
34.754600.
38.253700.
41.257800.
43.860900.
46.1211000.
48.0931100.
49.8091200.
51.3071300.
52.6151400.
53.7601500.
56.051750.
57.702000.
58.942250.
59.872500.
60.72750.
61.23000.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
24.441 ± 0.048371.2Stromsoe E., 1970Ideal 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
25.64 ± 0.23375.45
25.97 ± 0.23383.05
26.15 ± 0.23387.15
25.440 ± 0.050391.2
26.58 ± 0.23396.95
27.15 ± 0.23409.95
26.391 ± 0.053411.2
27.62 ± 0.23420.75
27.72 ± 0.23422.95
27.330 ± 0.055431.2
28.37 ± 0.23437.95
28.351 ± 0.057451.2
29.38 ± 0.23461.05
30.01 ± 0.23475.35
31.30 ± 0.23504.95
31.60 ± 0.23511.85
32.50 ± 0.23532.35
33.71 ± 0.23560.05
34.53 ± 0.23578.85
35.60 ± 0.23603.25

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-72.309 ± 0.060kcal/molCcbMosselman and Dekker, 1975ALS
ΔfH°liquid-72.42 ± 0.31kcal/molEqkConnett, 1972ALS
ΔfH°liquid-72.79 ± 0.09kcal/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
ΔfH°liquid-72.3 ± 1.0kcal/molCcbSnelson and Skinner, 1961ALS
ΔfH°liquid-73.20 ± 0.24kcal/molCcbGreen, 1960ALS
Quantity Value Units Method Reference Comment
ΔcH°liquid-483.105 ± 0.060kcal/molCcbMosselman and Dekker, 1975Corresponding ΔfHºliquid = -72.309 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
ΔcH°liquid-482.64 ± 0.07kcal/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding ΔfHºliquid = -72.77 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
ΔcH°liquid-483.12 ± 0.18kcal/molCcbSnelson and Skinner, 1961Corresponding ΔfHºliquid = -72.29 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
ΔcH°liquid-482.23 ± 0.24kcal/molCcbGreen, 1960Corresponding ΔfHºliquid = -73.18 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
ΔcH°liquid-485.801kcal/molCcbRichards and Davis, 1920At 291 K; Corresponding ΔfHºliquid = -69.613 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
S°liquid46.08cal/mol*KN/ACounsell, Lees, et al., 1968DH
S°liquid51.20cal/mol*KN/AParks and Huffman, 1926Extrapolation below 90 K, 64.85 J/mol*K.; DH
Quantity Value Units Method Reference Comment
S°solid,1 bar26.94cal/mol*KN/ACounsell, Lees, et al., 1968glass phase; DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
34.56298.Korolev, Kukharenko, et al., 1986DH
34.407298.15Tanaka, Toyama, et al., 1986DH
34.522298.15Zegers and Somsen, 1984DH
33.078288.15Benson and D'Arcy, 1982DH
35.105298.15Villamanan, Casanova, et al., 1982DH
33.89293.15Arutyunyan, Bagdasaryan, et al., 1981T = 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
34.976298.216Kalinowska, Jedlinska, et al., 1980T = 185 to 300 K. Unsmoothed experimental datum.; DH
35.35303.4Griigo'ev, Yanin, et al., 1979T = 303 to 463 K. p = 0.98 bar.; DH
34.362298.15Vesely, Zabransky, et al., 1979DH
35.61298.15Murthy and Subrahmanyam, 1977DH
34.364298.15Vesely, Svoboda, et al., 1977DH
34.386298.15Fortier, Benson, et al., 1976DH
34.4316298.15Fortier and Benson, 1976DH
37.91313.2Paz Andrade, Paz, et al., 1970DH
34.37298.15Counsell, Lees, et al., 1968T = 11 to 350 K.; DH
34.92298.Recko, 1968T = 24 to 40°C, equation only.; DH
37.19320.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 74°C.; DH
33.511303.Eucken and Eigen, 1951T = 303 to 393 K.; DH
34.80298.1Zhdanov, 1941T = 5 to 46°C.; DH
39.39301.2Phillip, 1939DH
32.50270.Mitsukuri and Hara, 1929T = 170 to 270 K.; DH
46.10298.1Parks, Kelley, et al., 1929Extrapolation below 90 K, 43.5 J/mol*K. Revision of previous data.; DH
31.91275.4Parks and Huffman, 1927T = 86 to 275 K. Value is unsmoothed experimental datum.; DH
31.91275.0Parks and Huffman, 1926T = 86 to 275 K. Value is unsmoothed experimental datum.; DH
31.38274.6Gibson, Parks, et al., 1920T = 77 to 274.6 K. Unsmoothed experimental datum.; DH
34.61298.von Reis, 1881T = 289 to 363 K.; DH

Constant pressure heat capacity of solid

Cp,solid (cal/mol*K) Temperature (K) Reference Comment
25.41150.Counsell, Lees, et al., 1968glass 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
Tboil370.3 ± 0.5KAVGN/AAverage of 127 out of 139 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus146.7KN/ATschamler, Richter, et al., 1949Uncertainty assigned by TRC = 0.5 K; TRC
Tfus147.KN/ATimmermans, 1935Uncertainty assigned by TRC = 3. K; TRC
Quantity Value Units Method Reference Comment
Ttriple148.75KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.02 K; TRC
Ttriple148.75KN/ACounsell, Lees, et al., 1968, 2Uncertainty assigned by TRC = 0.02 K; TRC
Ttriple147.0KN/AParks and Huffman, 1926, 2Uncertainty assigned by TRC = 0.3 K; TRC
Quantity Value Units Method Reference Comment
Tc536.9 ± 0.8KAVGN/AAverage of 20 out of 25 values; Individual data points
Quantity Value Units Method Reference Comment
Pc51. ± 1.atmAVGN/AAverage of 12 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.218l/molN/AGude and Teja, 1995 
Vc0.216l/molN/AZawisza and Vejrosta, 1982Uncertainty assigned by TRC = 0.001 l/mol; Visual; TRC
Quantity Value Units Method Reference Comment
ρc4.58 ± 0.06mol/lAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
ΔvapH°11.3 ± 0.4kcal/molAVGN/AAverage of 15 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
9.904370.3N/AMajer and Svoboda, 1985 
9.85371.N/AWormald and Vine, 2000AC
8.41423.N/AWormald and Vine, 2000AC
7.03453.N/AWormald and Vine, 2000AC
5.02498.N/AWormald and Vine, 2000AC
2.72528.N/AWormald and Vine, 2000AC
11.2318.N/AAucejo, Gonzalez-Alfaro, et al., 1995Based on data from 303. to 370. K.; AC
10.3375.N/AOrtega, Susial, et al., 1990Based on data from 360. to 377. K.; AC
11.5214.AStephenson and Malanowski, 1987Based on data from 200. to 228. K.; AC
10.4366.AStephenson and Malanowski, 1987Based on data from 356. to 376. K.; AC
10.1384.AStephenson and Malanowski, 1987Based on data from 369. to 407. K.; AC
9.58416.AStephenson and Malanowski, 1987Based on data from 401. to 482. K.; AC
8.72492.AStephenson and Malanowski, 1987Based on data from 478. to 507. K.; AC
11.1 ± 0.02313.CSvoboda, Veselý, et al., 1973AC
10.9 ± 0.02323.CSvoboda, Veselý, et al., 1973AC
10.7 ± 0.02333.CSvoboda, Veselý, et al., 1973AC
10.5 ± 0.02343.CSvoboda, Veselý, et al., 1973AC
10.3 ± 0.02353.CSvoboda, Veselý, et al., 1973AC
10.1 ± 0.02363.CSvoboda, Veselý, et al., 1973AC
11.8290.N/AWilhoit and Zwolinski, 1973Based on data from 275. to 373. K.; AC
10.7348.EBAmbrose, Counsell, et al., 1970Based on data from 333. to 377. K. See also Stephenson and Malanowski, 1987.; AC
11.2307.DTAKemme and Kreps, 1969Based on data from 292. to 370. K.; AC
11.2303.N/AVan Ness, Soczek, et al., 1967Based on data from 288. to 348. K.; AC
9.73420.N/AAmbrose and Townsend, 1963Based on data from 405. to 537. K.; AC
10.6353.EBBiddiscombe, Collerson, et al., 1963Based on data from 338. to 378. K.; AC
10.5358.N/AMathews and McKetta, 1961Based on data from 343. to 385. K.; AC
10.5 ± 0.02343.CMathews and McKetta, 1961AC
10.1 ± 0.02360.CMathews and McKetta, 1961AC
9.85 ± 0.02370.CMathews and McKetta, 1961AC
9.63 ± 0.02378.CMathews and McKetta, 1961AC
9.49 ± 0.02384.CMathews and McKetta, 1961AC
10.9321. to 367.N/AAronovich, Kastorskii, et al., 1959AC
10.3354.N/AWilliamson and Harrison, 1957AC
10.75 ± 0.10333.13VWilliamson and Harrison, 1957, 2ALS

Enthalpy of vaporization

ΔvapH = A exp(-αTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kcal/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 298. to 390.
A (kcal/mol) 12.44
α -0.8386
β 0.6888
Tc (K) 536.7
ReferenceMajer and Svoboda, 1985

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (atm)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
333.32 to 377.724.870301441.629-74.299Ambrose and Sprake, 1970Coefficents calculated by NIST from author's data.
292.4 to 370.55.308131690.864-51.804Kemme and Kreps, 1969 
405.46 to 536.714.593001300.491-86.364Ambrose and Townsend, 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
1.284148.75Counsell, Lees, et al., 1968DH
1.3148.7van Miltenburg and van den Berg, 2004AC
1.28148.8Counsell, Lees, et al., 1968, 2AC
1.241147.0Parks and Huffman, 1926DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
8.630148.75Counsell, Lees, et al., 1968DH
8.44147.0Parks and Huffman, 1926DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:

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

C3H9O+ + 1-Propanol = (C3H9O+ • 1-Propanol)

By formula: C3H9O+ + C3H8O = (C3H9O+ • C3H8O)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
ΔrH°30.4kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; switching reaction(CH3CNH+)CH3CN; Lias, Liebman, et al., 1984, Deakyne, Meot-Ner (Mautner), et al., 1986; M
ΔrH°31.6kcal/molICRLarson and McMahon, 1982gas 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°26.7cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; switching reaction(CH3CNH+)CH3CN; Lias, Liebman, et al., 1984, Deakyne, Meot-Ner (Mautner), et al., 1986; M
ΔrS°30.2cal/mol*KN/ALarson and McMahon, 1982gas 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°22.6kcal/molICRLarson and McMahon, 1982gas 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

C2H7O+ + 1-Propanol = (C2H7O+ • 1-Propanol)

By formula: C2H7O+ + C3H8O = (C2H7O+ • C3H8O)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
ΔrH°30.3kcal/molICRLarson and McMahon, 1982gas 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°28.4cal/mol*KN/ALarson and McMahon, 1982gas 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°21.8kcal/molICRLarson and McMahon, 1982gas 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

C4H11O+ + 1-Propanol = (C4H11O+ • 1-Propanol)

By formula: C4H11O+ + C3H8O = (C4H11O+ • C3H8O)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
ΔrH°31.7kcal/molICRLarson and McMahon, 1982gas 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°29.2cal/mol*KN/ALarson and McMahon, 1982gas 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°23.0kcal/molICRLarson and McMahon, 1982gas 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- + Hydrogen cation = 1-Propanol

By formula: C3H7O- + H+ = C3H8O

Quantity Value Units Method Reference Comment
ΔrH°375.7 ± 1.3kcal/molD-EAEllison, Engleking, et al., 1982gas phase; B
ΔrH°376.0 ± 2.1kcal/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
ΔrH°376.2 ± 2.0kcal/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Quantity Value Units Method Reference Comment
ΔrG°369.2 ± 1.4kcal/molH-TSEllison, Engleking, et al., 1982gas phase; B
ΔrG°369.4 ± 2.0kcal/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
ΔrG°369.6 ± 2.1kcal/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B

C4H9O- + 1-Propanol = (C4H9O- • 1-Propanol)

By formula: C4H9O- + C3H8O = (C4H9O- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°27.3 ± 2.9kcal/molN/ACaldwell, Rozeboom, et al., 1984gas 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°29.3cal/mol*KN/ACaldwell, Rozeboom, et al., 1984gas 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°18.6 ± 2.0kcal/molIMRECaldwell, Rozeboom, et al., 1984gas 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

C8H5- + 1-Propanol = (C8H5- • 1-Propanol)

By formula: C8H5- + C3H8O = (C8H5- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°22.5 ± 2.9kcal/molN/ACaldwell, Rozeboom, et al., 1984gas 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°29.3cal/mol*KN/ACaldwell, Rozeboom, et al., 1984gas 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°13.8 ± 2.0kcal/molIMRECaldwell, Rozeboom, et al., 1984gas 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

C3H7O- + 1-Propanol = (C3H7O- • 1-Propanol)

By formula: C3H7O- + C3H8O = (C3H7O- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°28.5 ± 2.9kcal/molN/ACaldwell, Rozeboom, et al., 1984gas 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°29.3cal/mol*KN/ACaldwell, Rozeboom, et al., 1984gas 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°19.4 ± 2.0kcal/molIMRECaldwell, Rozeboom, et al., 1984gas 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

Chlorine anion + 1-Propanol = (Chlorine anion • 1-Propanol)

By formula: Cl- + C3H8O = (Cl- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°20.40 ± 0.50kcal/molTDAsHiraoka, 1987gas phase; B,B,M
ΔrH°17.7 ± 2.0kcal/molIMRELarson and McMahon, 1984gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°29.0cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
ΔrS°23.2cal/mol*KN/ALarson and McMahon, 1984gas phase; switching reaction(Cl-)t-C4H9OH, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M
Quantity Value Units Method Reference Comment
ΔrG°11.70kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B
ΔrG°11.7 ± 2.0kcal/molTDAsHiraoka, 1987gas phase; B
ΔrG°10.8 ± 2.0kcal/molIMRELarson and McMahon, 1984gas phase; B,M

C3H5O+ + 1-Propanol = (C3H5O+ • 1-Propanol)

By formula: C3H5O+ + C3H8O = (C3H5O+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°21.7kcal/molICRCaldwell, Rozeboom, et al., 1984gas 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°29.3cal/mol*KN/ACaldwell, Rozeboom, et al., 1984gas 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°13.0kcal/molICRCaldwell, Rozeboom, et al., 1984gas phase; switching reaction(CH3O-)CH3OH, Entropy change calculated or estimated; re-evaluated using Meot-Ner(Mautner), 1986 and Paul and Kebarle, 1990; M

C3H9Si+ + 1-Propanol = (C3H9Si+ • 1-Propanol)

By formula: C3H9Si+ + C3H8O = (C3H9Si+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°43.3kcal/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+))H2O, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
ΔrS°30.8cal/mol*KN/AWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+))H2O, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
28.9468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+))H2O, Entropy change calculated or estimated; M

C3H9Sn+ + 1-Propanol = (C3H9Sn+ • 1-Propanol)

By formula: C3H9Sn+ + C3H8O = (C3H9Sn+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°35.5kcal/molPHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
ΔrS°32.cal/mol*KN/AStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
18.7525.PHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

C5H11O- + 1-Propanol = (C5H11O- • 1-Propanol)

By formula: C5H11O- + C3H8O = (C5H11O- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°26.9 ± 2.9kcal/molN/ACaldwell, Rozeboom, et al., 1984gas 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°18.2 ± 2.0kcal/molIMRECaldwell, Rozeboom, et al., 1984gas 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

C3H5O- + 1-Propanol = (C3H5O- • 1-Propanol)

By formula: C3H5O- + C3H8O = (C3H5O- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°21.6 ± 2.9kcal/molN/ACaldwell, Rozeboom, et al., 1984gas 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°12.9 ± 2.0kcal/molIMRECaldwell, Rozeboom, et al., 1984gas 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

(C3H9O+ • 71-Propanol) + 1-Propanol = (C3H9O+ • 81-Propanol)

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°11.kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
ΔrS°30.cal/mol*KN/AMeot-Ner (Mautner), 1992gas phase; Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
4.1215.PHPMSMeot-Ner (Mautner), 1992gas phase; Entropy change calculated or estimated; M

(Chlorine anion • 71-Propanol) + 1-Propanol = (Chlorine anion • 81-Propanol)

By formula: (Cl- • 7C3H8O) + C3H8O = (Cl- • 8C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°10.8 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; Estimated entropy; single temperature measurement; B,M
Quantity Value Units Method Reference Comment
ΔrS°30.cal/mol*KN/AHiraoka and Mizuse, 1987gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
ΔrG°1.8 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; Estimated entropy; single temperature measurement; B

Fluorine anion + 1-Propanol = (Fluorine anion • 1-Propanol)

By formula: F- + C3H8O = (F- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°32.3 ± 2.0kcal/molIMRELarson and McMahon, 1983gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°25.4cal/mol*KN/ALarson and McMahon, 1983gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M
Quantity Value Units Method Reference Comment
ΔrG°24.7 ± 2.0kcal/molIMRELarson and McMahon, 1983gas phase; B,M

(C3H9O+ • 21-Propanol) + 1-Propanol = (C3H9O+ • 31-Propanol)

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°14.4kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrH°14.2kcal/molPHPMSHiraoka, Morise, et al., 1986gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°25.5cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrS°23.8cal/mol*KPHPMSHiraoka, Morise, et al., 1986gas phase; M

(C3H9O+ • 31-Propanol) + 1-Propanol = (C3H9O+ • 41-Propanol)

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°11.9kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrH°11.7kcal/molPHPMSHiraoka, Morise, et al., 1986gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°24.8cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrS°23.0cal/mol*KPHPMSHiraoka, Morise, et al., 1986gas phase; M

(C3H9O+ • 1-Propanol) + 1-Propanol = (C3H9O+ • 21-Propanol)

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°21.6kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrH°18.9kcal/molPHPMSHiraoka, Morise, et al., 1986gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°31.4cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M
ΔrS°23.0cal/mol*KPHPMSHiraoka, Morise, et al., 1986gas phase; M

Propanal + Hydrogen = 1-Propanol

By formula: C3H6O + H2 = C3H8O

Quantity Value Units Method Reference Comment
ΔrH°-20.14 ± 0.09kcal/molCmWiberg, Crocker, et al., 1991liquid phase; solvent: Triglyme; Heat of hydrogenation; ALS
ΔrH°-16.62 ± 0.18kcal/molEqkConnett, 1972gas phase; At 473-524 K; ALS
ΔrH°-15.72 ± 0.16kcal/molChydBuckley and Cox, 1967gas phase; ALS

(Chlorine anion • 21-Propanol) + 1-Propanol = (Chlorine anion • 31-Propanol)

By formula: (Cl- • 2C3H8O) + C3H8O = (Cl- • 3C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°14.2 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°31.2cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°4.8 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 31-Propanol) + 1-Propanol = (Chlorine anion • 41-Propanol)

By formula: (Cl- • 3C3H8O) + C3H8O = (Cl- • 4C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°13.3 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°32.1cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°3.7 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 41-Propanol) + 1-Propanol = (Chlorine anion • 51-Propanol)

By formula: (Cl- • 4C3H8O) + C3H8O = (Cl- • 5C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°12.6 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°32.9cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°2.7 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 51-Propanol) + 1-Propanol = (Chlorine anion • 61-Propanol)

By formula: (Cl- • 5C3H8O) + C3H8O = (Cl- • 6C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°11.6 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°31.0cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°2.3 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 61-Propanol) + 1-Propanol = (Chlorine anion • 71-Propanol)

By formula: (Cl- • 6C3H8O) + C3H8O = (Cl- • 7C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°11.0 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°30.2cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°1.9 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 1-Propanol) + 1-Propanol = (Chlorine anion • 21-Propanol)

By formula: (Cl- • C3H8O) + C3H8O = (Cl- • 2C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°15.8 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
ΔrS°25.4cal/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
ΔrG°8.2 ± 1.0kcal/molTDAsHiraoka and Mizuse, 1987gas phase; B

(C3H9O+ • 41-Propanol) + 1-Propanol = (C3H9O+ • 51-Propanol)

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°10.9kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°25.4cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M

(C3H9O+ • 51-Propanol) + 1-Propanol = (C3H9O+ • 61-Propanol)

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°11.1kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°28.8cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M

(C3H9O+ • 61-Propanol) + 1-Propanol = (C3H9O+ • 71-Propanol)

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°10.9kcal/molPHPMSMeot-Ner (Mautner), 1992gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°30.5cal/mol*KPHPMSMeot-Ner (Mautner), 1992gas phase; M

CH6N+ + 1-Propanol = (CH6N+ • 1-Propanol)

By formula: CH6N+ + C3H8O = (CH6N+ • C3H8O)

Bond type: Hydrogen bonds of the type NH+-O between organics

Quantity Value Units Method Reference Comment
ΔrH°22.0kcal/molPHPMSMeot-Ner, 1984gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°25.6cal/mol*KPHPMSMeot-Ner, 1984gas phase; M

Sodium ion (1+) + 1-Propanol = (Sodium ion (1+) • 1-Propanol)

By formula: Na+ + C3H8O = (Na+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°25.8 ± 1.0kcal/molCIDTArmentrout and Rodgers, 2000RCD
ΔrH°25.8 ± 1.0kcal/molCIDTRodgers and Armentrout, 1999RCD

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
0.00.CIDTRodgers and Armentrout, 1999RCD

2-Propen-1-ol + Hydrogen = 1-Propanol

By formula: C3H6O + H2 = C3H8O

Quantity Value Units Method Reference Comment
ΔrH°-31.22 ± 0.42kcal/molChydDolliver, Gresham, et al., 1938gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -31.5 ± 0.3 kcal/mol; At 355°K; ALS

thiophenoxide anion + 1-Propanol = (thiophenoxide anion • 1-Propanol)

By formula: C6H5S- + C3H8O = (C6H5S- • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°15.0kcal/molPHPMSSieck and Meot-ner, 1989gas phase; M
Quantity Value Units Method Reference Comment
ΔrS°26.0cal/mol*KPHPMSSieck and Meot-ner, 1989gas phase; M

Fluorine anion + 1-Propanol = C3H7D8FO-

By formula: F- + C3H8O = C3H7D8FO-

Quantity Value Units Method Reference Comment
ΔrG°24.3 ± 2.0kcal/molIMREWilkinson, Szulejko, et al., 1992gas phase; Reported relative to ROH..F-, 0.5 kcal/mol weaker.; B

Magnesium ion (1+) + 1-Propanol = (Magnesium ion (1+) • 1-Propanol)

By formula: Mg+ + C3H8O = (Mg+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°64. ± 5.kcal/molICROperti, Tews, et al., 1988gas phase; switching reaction,Thermochemical ladder(Mg+)CH3OH; M

Propyl gallate + Water = Benzoic acid, 3,4,5-trihydroxy- + 1-Propanol

By formula: C10H12O5 + H2O = C7H6O5 + C3H8O

Quantity Value Units Method Reference Comment
ΔrH°-3.7 ± 1.6kcal/molEqkTewari, Schantz, et al., 1996liquid phase; solvent: Toluene; ALS

1-Propanol + Ethene, 1,1-dichloro-2,2-difluoro- = C5H8Cl2F2O

By formula: C3H8O + C2Cl2F2 = C5H8Cl2F2O

Quantity Value Units Method Reference Comment
ΔrH°-39.1 ± 0.4kcal/molCmKennedy, Lacher, et al., 1969gas phase; ALS

1-Propanol + Nitric acid = Nitric acid, propyl ester + Water

By formula: C3H8O + HNO3 = C3H7NO3 + H2O

Quantity Value Units Method Reference Comment
ΔrH°-5.21kcal/molEqkRubtsov, 1986liquid phase; ALS

Ketene + 1-Propanol = n-Propyl acetate

By formula: C2H2O + C3H8O = C5H10O2

Quantity Value Units Method Reference Comment
ΔrH°-35.32kcal/molCmRice and Greenberg, 1934gas phase; ALS

Lithium ion (1+) + 1-Propanol = (Lithium ion (1+) • 1-Propanol)

By formula: Li+ + C3H8O = (Li+ • C3H8O)

Quantity Value Units Method Reference Comment
ΔrH°40.9 ± 1.9kcal/molCIDTRodgers and Armentrout, 2000RCD

Maleic anhydride + 1-Propanol = propyl hydrogen maleate

By formula: C4H2O3 + C3H8O = propyl hydrogen maleate

Quantity Value Units Method Reference Comment
ΔrH°-8.4kcal/molKinTribunescu, Poraicu, et al., 1978liquid 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. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
130.7500.MN/A 
150. CN/A 
160. MN/A 
140. MButler, Ramchandani, et al., 1935This 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
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Benson and D'Arcy, 1982
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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
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Notes

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