Isopropyl Alcohol

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-272.8kJ/molEqkBuckley and Herington, 1965ALS
Δfgas-271.1kJ/molN/AChao and Rossini, 1965Value 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
Δfgas-272.3 ± 0.92kJ/molCcbSnelson and Skinner, 1961ALS
Δfgas-272.8kJ/molN/AParks, Mosley, et al., 1950Value 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
35.3250.Thermodynamics Research Center, 1997p=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
46.04100.
57.98150.
68.28200.
83.72273.15
89.32 ± 0.15298.15
89.74300.
112.15400.
131.96500.
148.30600.
161.75700.
173.04800.
182.67900.
190.971000.
198.161100.
204.411200.
209.851300.
214.601400.
218.751500.
227.01750.
233.12000.
237.62250.
241.02500.
243.72750.
245.73000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
103.06358.72Stromsoe 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 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 ± 1.6365.75
105.77371.15
106.29373.15
108.1 ± 1.6378.85
109.2 ± 1.6384.95
110.08391.15
110.8 ± 1.6393.65
111.65398.15
113.0 ± 1.6405.35
114.35411.15
117.02423.15
118.70431.15
122.10448.15
122.80451.15
121.7 ± 1.6453.15
124.2 ± 1.6466.75
127.01473.15
126.7 ± 1.6480.55
130.3 ± 1.6499.75
132.9 ± 1.6513.95
137.5 ± 1.6539.05
142.6 ± 1.6567.05
148.1 ± 1.6597.25

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
Δfliquid-317.0 ± 0.3kJ/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
Δfliquid-318.2 ± 0.71kJ/molCcbSnelson and Skinner, 1961ALS
Δfliquid-318.7kJ/molCcbParks, Mosley, et al., 1950see Parks and Moore, 1939; ALS
Quantity Value Units Method Reference Comment
Δcliquid-2006.9 ± 0.2kJ/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding Δfliquid = -316.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2005.8 ± 0.4kJ/molCcbSnelson and Skinner, 1961Corresponding Δfliquid = -318.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2005.1kJ/molCcbParks, Mosley, et al., 1950see Parks and Moore, 1939; Corresponding Δfliquid = -318.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid180.58J/mol*KN/AAndon, Counsell, et al., 1963DH
liquid179.9J/mol*KN/AKelley, 1929DH
liquid192.9J/mol*KN/AParks and Kelley, 1928Extrapolation below 70 K, 43.56 J/mol*K.; DH
liquid190.8J/mol*KN/AParks and Kelley, 1925Extrapolation below 90 K, 53.22 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
161.2298.15Roux, Roberts, et al., 1980DH
154.75298.15Brown and Ziegler, 1979T = 185 to 304 K. Results as equation only.; DH
165.6311.6Griigo'ev, Yanin, et al., 1979T = 311 to 453 K. p = 0.98 bar.; DH
154.43298.15Andon, Counsell, et al., 1963T = 10 to 330 K.; DH
162.8298.2Katayama, 1962T = 10 to 60°C.; DH
180.3324.Swietoslawski and Zielenkiewicz, 1958Mean value 21 to 81°C.; DH
154.0298.Ginnings and Corruccini, 1948T = 0 to 200°C.; DH
159.99298.04Zhdanov, 1945T = 7 to 41°C. Value is unsmoothed experimental datum.; DH
172.4303.2Phillip, 1939DH
163.6298.Trew and Watkins, 1933DH
149.75292.84Kelley, 1929T = 16 to 298 K. Value is unsmoothed experimental datum.; DH
180.3298.1Parks, Kelley, et al., 1929Extrapolation below 90 K, 42.68 J/mol*K.; DH
151.0293.1Parks and Kelley, 1928T = 71 to 293 K. Value is unsmoothed experimental datum.; DH
152.3293.1Parks and Kelley, 1925T = 71 to 293 K. Value is unsmoothed experimental datum.; DH
169.9303.Willams and Daniels, 1924T = 303 to 323 K. Equation only.; 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
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil355.5 ± 0.4KAVGN/AAverage of 102 out of 118 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus185.75KN/AOgimachi, Corcoran, et al., 1961Uncertainty assigned by TRC = 0.5 K; TRC
Tfus185.35KN/AAnonymous, 1958TRC
Quantity Value Units Method Reference Comment
Ttriple184.9 ± 0.6KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tc509. ± 2.KAVGN/AAverage of 19 out of 20 values; Individual data points
Quantity Value Units Method Reference Comment
Pc49. ± 5.barAVGN/AAverage of 10 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.222l/molN/AGude and Teja, 1995 
Vc0.223l/molN/AAmbrose, Counsell, et al., 1978Uncertainty assigned by TRC = 0.003 l/mol; PVT compatible with values chosen.; TRC
Quantity Value Units Method Reference Comment
ρc4.51 ± 0.02mol/lN/AGude and Teja, 1995 
ρc4.54mol/lN/ATeja, Lee, et al., 1989TRC
ρc4.538mol/lN/AAmbrose and Townsend, 1963TRC
Quantity Value Units Method Reference Comment
Δvap45. ± 3.kJ/molAVGN/AAverage of 11 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
39.85355.4N/AMajer and Svoboda, 1985 
43.2337.N/ASegura, Galindo, et al., 2002Based on data from 322. to 355. K.; AC
39.8355.N/AWormald and Vine, 2000AC
29.7423.N/AWormald and Vine, 2000AC
23.7453.N/AWormald and Vine, 2000AC
16.5483.N/AWormald and Vine, 2000AC
10.5503.N/AWormald and Vine, 2000AC
44.8315.N/AAucejo, Gonzalez-Alfaro, et al., 1995Based on data from 300. to 355. K.; AC
50.3213.AStephenson and Malanowski, 1987Based on data from 195. to 228. K.; AC
42.0355.AStephenson and Malanowski, 1987Based on data from 347. to 368. K.; AC
41.3365.AStephenson and Malanowski, 1987Based on data from 350. to 383. K.; AC
39.2394.AStephenson and Malanowski, 1987Based on data from 379. to 461. K.; AC
35.3468.AStephenson and Malanowski, 1987Based on data from 453. to 508. K.; AC
43.1340.A,EBStephenson and Malanowski, 1987Based on data from 325. to 362. K. See also Ambrose, Counsell, et al., 1970.; AC
45.7288.N/AWilhoit and Zwolinski, 1973Based on data from 273. to 374. K.; AC
45.5303.N/AVan Ness, Soczek, et al., 1967Based on data from 288. to 348. K.; AC
42.7 ± 0.1330.CBerman, Larkam, et al., 1964AC
41.0 ± 0.1346.CBerman, Larkam, et al., 1964AC
39.8 ± 0.1355.CBerman, Larkam, et al., 1964AC
38.9 ± 0.1363.CBerman, Larkam, et al., 1964AC
39.1410.N/AAmbrose and Townsend, 1963, 2Based on data from 395. to 508. K.; AC
42.8344.EBBiddiscombe, Collerson, et al., 1963Based on data from 329. to 363. K.; AC
43.2324.CHales, Cox, et al., 1963AC
41.7339.CHales, Cox, et al., 1963AC
39.8355.CHales, Cox, et al., 1963AC
43.40 ± 0.08324.11VWilliamson and Harrison, 1957ALS
41.1369.N/AFoz Gazulla, Morcilio, et al., 1955Based 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)

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Temperature (K) 298. to 380.
A (kJ/mol) 53.38
α -0.708
β 0.6538
Tc (K) 508.3
ReferenceMajer 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
395.1 to 508.244.577951221.423-87.474Ambrose and Townsend, 1963, 3Coefficents calculated by NIST from author's data.
329.92 to 362.414.86101357.427-75.814Biddiscombe, Collerson, et al., 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
5.410185.20Andon, Counsell, et al., 1963DH
5.372184.67Kelley, 1929DH
5.41185.2Domalski and Hearing, 1996AC
5.301184.6Parks and Kelley, 1928DH
5.297184.6Parks and Kelley, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
29.21185.20Andon, Counsell, et al., 1963DH
29.09184.67Kelley, 1929DH
28.72184.6Parks and Kelley, 1928DH
28.7184.6Parks and Kelley, 1925DH

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:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
RCD - Robert C. Dunbar

Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.

Individual Reactions

C3H7O- + Hydrogen cation = Isopropyl Alcohol

By formula: C3H7O- + H+ = C3H8O

Quantity Value Units Method Reference Comment
Δr1569. ± 4.2kJ/molD-EARamond, Davico, et al., 2000gas phase; B
Δr1571. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1576. ± 4.2kJ/molCIDTDeTuri and Ervin, 1999gas phase; B
Δr1572. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Quantity Value Units Method Reference Comment
Δr1542. ± 4.6kJ/molH-TSRamond, Davico, et al., 2000gas phase; B
Δr1543. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1544. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B

Chlorine anion + Isopropyl Alcohol = (Chlorine anion • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr81.17 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr76.6 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Δr73.6 ± 8.4kJ/molIMRELarson and McMahon, 1984gas phase; B,M
Quantity Value Units Method Reference Comment
Δr103.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Δr97.1J/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
Δr47.36kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr45.61kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B
Δr44.8 ± 8.4kJ/molIMRELarson and McMahon, 1984gas phase; B,M

C2H7O+ + Isopropyl Alcohol = (C2H7O+ • Isopropyl Alcohol)

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

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

Quantity Value Units Method Reference Comment
Δr133.kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr124.J/mol*KN/ABomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr96.7kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M

C3H9O+ + Isopropyl Alcohol = (C3H9O+ • Isopropyl Alcohol)

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

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

Quantity Value Units Method Reference Comment
Δr133.kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr124.J/mol*KN/ABomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr96.7kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M

C4H11O+ + Isopropyl Alcohol = (C4H11O+ • Isopropyl Alcohol)

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

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

Quantity Value Units Method Reference Comment
Δr128.kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr118.J/mol*KN/ABomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr92.5kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M

C4H11O+ + Isopropyl Alcohol = (C4H11O+ • Isopropyl Alcohol)

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

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

Quantity Value Units Method Reference Comment
Δr134.kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr115.J/mol*KN/ABomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr99.6kJ/molICRBomse and Beauchamp, 1981gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M

CN- + Isopropyl Alcohol = (CN- • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr69.9 ± 3.3kJ/molTDAsLarson, Szulejko, et al., 1988gas phase; B,M
Δr76. ± 15.kJ/molIMRELarson and McMahon, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr110.J/mol*KPHPMSLarson, Szulejko, et al., 1988gas phase; M
Δr104.J/mol*KN/ALarson and McMahon, 1987gas phase; switching reaction,Thermochemical ladder(CN-)H2O, Entropy change calculated or estimated; Payzant, Yamdagni, et al., 1971; M
Quantity Value Units Method Reference Comment
Δr37.7 ± 0.84kJ/molTDAsLarson, Szulejko, et al., 1988gas phase; B
Δr44.8 ± 9.6kJ/molIMRELarson and McMahon, 1987gas phase; B,M

Fluorine anion + Isopropyl Alcohol = (Fluorine anion • Isopropyl Alcohol)

By formula: F- + C3H8O = (F- • C3H8O)

Quantity Value Units Method Reference Comment
Δr140.2 ± 2.9kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr135. ± 8.4kJ/molIMRELarson and McMahon, 1983gas phase; B,M
Δr139. ± 9.2kJ/molCIDTDeTuri and Ervin, 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr107.J/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
Δr107.5kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr103. ± 8.4kJ/molIMRELarson and McMahon, 1983gas phase; B,M

C3H9Si+ + Isopropyl Alcohol = (C3H9Si+ • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr184.kJ/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr129.J/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° (kJ/mol) T (K) Method Reference Comment
123.468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M

(Chlorine anion • 2Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 3Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr62.3 ± 2.1kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr52.3 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr109.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr22.2kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr20. ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 2Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr69.9 ± 1.3kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr65.3 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr105.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr32.1kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr34. ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 7Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 8Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr45.6 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; Estimated entropy; single temperature measurement; B,M
Quantity Value Units Method Reference Comment
Δr130.J/mol*KN/AHiraoka and Mizuse, 1987gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr6.7 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; Estimated entropy; single temperature measurement; B

Iodide + Isopropyl Alcohol = (Iodide • Isopropyl Alcohol)

By formula: I- + C3H8O = (I- • C3H8O)

Quantity Value Units Method Reference Comment
Δr54.81 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr51.0 ± 4.2kJ/molTDAsCaldwell and Kebarle, 1984gas phase; B,M
Quantity Value Units Method Reference Comment
Δr79.9J/mol*KPHPMSCaldwell and Kebarle, 1984gas phase; M
Quantity Value Units Method Reference Comment
Δr26.5kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr27. ± 4.2kJ/molTDAsCaldwell and Kebarle, 1984gas phase; B

Hydrogen + Acetone = Isopropyl Alcohol

By formula: H2 + C3H6O = C3H8O

Quantity Value Units Method Reference Comment
Δr-68.74 ± 0.42kJ/molCmWiberg, Crocker, et al., 1991liquid phase; ALS
Δr-55.23kJ/molEqkBuckley and Herington, 1965gas phase; ALS
Δr-55.40 ± 0.42kJ/molChydDolliver, Gresham, et al., 1938gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -56.1 ± 0.4 kJ/mol; At 355 °K; ALS

Bromine anion + Isopropyl Alcohol = C3H8BrO-

By formula: Br- + C3H8O = C3H8BrO-

Quantity Value Units Method Reference Comment
Δr60.25 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr34.9kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Δr38. ± 8.4kJ/molIMRETanabe, Morgon, et al., 1996gas phase; Anchored to H2O..Br- of Hiraoka, Mizure, et al., 19882; B

Sodium ion (1+) + Isopropyl Alcohol = (Sodium ion (1+) • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr113. ± 4.2kJ/molCIDTArmentrout and Rodgers, 2000RCD
Δr113. ± 4.6kJ/molCIDTRodgers and Armentrout, 1999RCD

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
85.4298.IMREMcMahon and Ohanessian, 2000Anchor alanine=39.89; RCD
0.00.CIDTRodgers and Armentrout, 1999RCD

(Chlorine anion • 3Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 4Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr49.8 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr120.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr14. ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 4Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 5Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr48.5 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr128.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr10. ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 5Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 6Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr47.3 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr130.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr8.4 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

(Chlorine anion • 6Isopropyl Alcohol) + Isopropyl Alcohol = (Chlorine anion • 7Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr46.4 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B,M
Quantity Value Units Method Reference Comment
Δr131.J/mol*KPHPMSHiraoka and Mizuse, 1987gas phase; M
Quantity Value Units Method Reference Comment
Δr7.1 ± 4.2kJ/molTDAsHiraoka and Mizuse, 1987gas phase; B

MeS anion + Isopropyl Alcohol = (MeS anion • Isopropyl Alcohol)

By formula: CH3S- + C3H8O = (CH3S- • C3H8O)

Quantity Value Units Method Reference Comment
Δr71.55 ± 0.84kJ/molTDAsSieck and Meot-ner, 1989gas phase; B,M
Quantity Value Units Method Reference Comment
Δr96.7J/mol*KPHPMSSieck and Meot-ner, 1989gas phase; M
Quantity Value Units Method Reference Comment
Δr42.7 ± 3.3kJ/molTDAsSieck and Meot-ner, 1989gas phase; B

Fluorine anion + 2Isopropyl Alcohol = C6H16FO2-

By formula: F- + 2C3H8O = C6H16FO2-

Quantity Value Units Method Reference Comment
Δr87.03 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr55.48kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B

thiophenoxide anion + Isopropyl Alcohol = C9H13OS-

By formula: C6H5S- + C3H8O = C9H13OS-

Quantity Value Units Method Reference Comment
Δr62.76 ± 0.42kJ/molTDAsSieck and Meot-ner, 1989gas phase; B
Quantity Value Units Method Reference Comment
Δr30.5 ± 1.7kJ/molTDAsSieck and Meot-ner, 1989gas phase; B

Fluorine anion + 3Isopropyl Alcohol = C9H24FO3-

By formula: F- + 3C3H8O = C9H24FO3-

Quantity Value Units Method Reference Comment
Δr73.64 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr35.0kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B

Iodide + 2Isopropyl Alcohol = C6H16IO2-

By formula: I- + 2C3H8O = C6H16IO2-

Quantity Value Units Method Reference Comment
Δr46.0 ± 1.3kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr19.5kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B

Bromine anion + 2Isopropyl Alcohol = C6H16BrO2-

By formula: Br- + 2C3H8O = C6H16BrO2-

Quantity Value Units Method Reference Comment
Δr51.46 ± 0.84kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr22.8kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B

Iodide + 3Isopropyl Alcohol = C9H24IO3-

By formula: I- + 3C3H8O = C9H24IO3-

Quantity Value Units Method Reference Comment
Δr39.7 ± 2.9kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr14.8kJ/molTDAsBogdanov, Peschke, et al., 1999gas phase; B

1-Propene, 2-methyl- + Isopropyl Alcohol = Propane, 2-methyl-2-(1-methylethoxy)-

By formula: C4H8 + C3H8O = C7H16O

Quantity Value Units Method Reference Comment
Δr-22.9 ± 1.3kJ/molEqkCalderon, Tejero, et al., 1997liquid phase; ALS
Δr-21.7 ± 1.6kJ/molCmSola, Pericas, et al., 1997liquid phase; ALS

Isopropyl Alcohol = Hydrogen + Acetone

By formula: C3H8O = H2 + C3H6O

Quantity Value Units Method Reference Comment
Δr55.23kJ/molEqkBuckley and Herington, 1965gas phase; ALS
Δr56.543kJ/molEqkKolb and Burwell, 1945gas phase; ALS

Fluorine anion + Isopropyl Alcohol = C3H7D8FO-

By formula: F- + C3H8O = C3H7D8FO-

Quantity Value Units Method Reference Comment
Δr102. ± 8.4kJ/molIMREWilkinson, Szulejko, et al., 1992gas phase; Reported relative to ROH..F-, 0.5 kcal/mol weaker.; B

Magnesium ion (1+) + Isopropyl Alcohol = (Magnesium ion (1+) • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr270. ± 20.kJ/molICROperti, Tews, et al., 1988gas phase; switching reaction,Thermochemical ladder(Mg+)CH3OH; M

Isopropyl acetate + Water = Acetic acid + Isopropyl Alcohol

By formula: C5H10O2 + H2O = C2H4O2 + C3H8O

Quantity Value Units Method Reference Comment
Δr2.3 ± 0.2kJ/molCmWadso, 1958liquid phase; Heat of Hydrolysis; ALS

Isopropyl Alcohol + Chloral = 2,2,2-trichloro-1-isopropoxyethanol

By formula: C3H8O + C2HCl3O = 2,2,2-trichloro-1-isopropoxyethanol

Quantity Value Units Method Reference Comment
Δr-41.6kJ/molEqkJensen and Pedersen, 1971liquid phase; solvent: Heptane; ALS

Cyclohexanol + Acetone = Cyclohexanone + Isopropyl Alcohol

By formula: C6H12O + C3H6O = C6H10O + C3H8O

Quantity Value Units Method Reference Comment
Δr9.9 ± 1.9kJ/molEqkFedoseenko, Yursha, et al., 1983gas phase; At 503 K; ALS

Isopropyl Alcohol + Ethene, 1,1-dichloro-2,2-difluoro- = C5H8Cl2F2O

By formula: C3H8O + C2Cl2F2 = C5H8Cl2F2O

Quantity Value Units Method Reference Comment
Δr-183. ± 1.kJ/molEqkKennedy, Lacher, et al., 1969gas phase; ALS

Cyclohexanone + Isopropyl Alcohol = Cyclohexanol + Acetone

By formula: C6H10O + C3H8O = C6H12O + C3H6O

Quantity Value Units Method Reference Comment
Δr-9.9 ± 1.9kJ/molEqkKabo, Yursha, et al., 1988gas phase; ALS

Isopropyl Alcohol + Nitric acid = Nitric acid, 1-methylethyl ester + Water

By formula: C3H8O + HNO3 = C3H7NO3 + H2O

Quantity Value Units Method Reference Comment
Δr-23.4kJ/molEqkRubtsov, 1986liquid phase; ALS

Ketene + Isopropyl Alcohol = Isopropyl acetate

By formula: C2H2O + C3H8O = C5H10O2

Quantity Value Units Method Reference Comment
Δr-150.2kJ/molCmRice and Greenberg, 1934liquid phase; ALS

Lithium ion (1+) + Isopropyl Alcohol = (Lithium ion (1+) • Isopropyl Alcohol)

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

Quantity Value Units Method Reference Comment
Δr173. ± 7.9kJ/molCIDTRodgers and Armentrout, 2000RCD

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) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
88. 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 
170. RN/A 
120. MButler, Ramchandani, et al., 1935 

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.

Buckley and Herington, 1965
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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]

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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]

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Notes

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