Formaldehyde

Data at NIST subscription sites:

NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.


Gas phase thermochemistry data

Go To: Top, 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 compiled as indicated in comments:
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
Δfgas-115.90kJ/molReviewChase, 1998Data last reviewed in March, 1961
Δfgas-108.6 ± 0.46kJ/molCmFletcher and Pilcher, 1970ALS
Quantity Value Units Method Reference Comment
Δcgas-570.78 ± 0.42kJ/molCmFletcher and Pilcher, 1970Corresponding Δfgas = -108.6 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcgas-561.1kJ/molCcbWartenberg and Lerner-Steinberg, 1925Gas phase; Corresponding Δfgas = -118. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
gas,1 bar218.95J/mol*KReviewChase, 1998Data last reviewed in March, 1961

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
33.2650.Thermodynamics Research Center, 1997p=1 bar. Recommended entropies and heat capacities are in good agreement with other statistically calculated values [ Thompson, 1941, Pillai M.G.K., 1961, Gurvich, Veyts, et al., 1989]. Please also see Chao J., 1980, Chao J., 1986.; GT
33.26100.
33.28150.
33.50200.
34.70273.15
35.39 ± 0.02298.15
35.44300.
39.24400.
43.74500.
48.18600.
52.28700.
55.94800.
59.16900.
61.951000.
64.371100.
66.451200.
68.251300.
69.801400.
71.151500.
73.791750.
75.682000.
77.082250.
78.132500.
78.932750.
79.563000.

Gas Phase Heat Capacity (Shomate Equation)

Cp° = A + B*t + C*t2 + D*t3 + E/t2
H° − H°298.15= A*t + B*t2/2 + C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 − E/(2*t2) + G
    Cp = heat capacity (J/mol*K)
    H° = standard enthalpy (kJ/mol)
    S° = standard entropy (J/mol*K)
    t = temperature (K) / 1000.

View plot Requires a JavaScript / HTML 5 canvas capable browser.

View table.

Temperature (K) 298. to 1200.1200. to 6000.
A 5.19376771.35268
B 93.232496.174497
C -44.85457-1.191090
D 7.8822790.079564
E 0.551175-15.58917
F -119.3591-170.6327
G 202.4663262.3180
H -115.8972-115.8972
ReferenceChase, 1998Chase, 1998
Comment Data last reviewed in March, 1961 Data last reviewed in March, 1961

Phase change data

Go To: Top, Gas phase thermochemistry data, References, Notes

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

Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos

Quantity Value Units Method Reference Comment
Tboil253.85KN/ASpence and Wild, 1935Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tfus181.KN/AAnonymous, 1958Uncertainty assigned by TRC = 4. K; TRC
Tfus181.KN/AHarries, 1901Uncertainty assigned by TRC = 6. K; TRC
Quantity Value Units Method Reference Comment
Ttriple155.1KN/ASpence and Wild, 1935Uncertainty assigned by TRC = 0.3 K; TRC

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
24.3236.AStephenson and Malanowski, 1987Based on data from 184. to 251. K.; AC
24.2236.N/ASpence and Wild, 1935, 2Based on data from 173. to 251. K. See also Stephenson and Malanowski, 1987.; AC

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
163.76 to 250.864.28176959.43-29.758Spence and Wild, 1935, 3Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
7.53155.Vasil'ev and Lebedev, 1998AC

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:


References

Go To: Top, Gas phase thermochemistry data, Phase change data, Notes

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

Chase, 1998
Chase, M.W., Jr., NIST-JANAF Themochemical Tables, Fourth Edition, J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]

Fletcher and Pilcher, 1970
Fletcher, R.A.; Pilcher, G., Measurements of heats of combustion by flame calorimetry, Trans. Faraday Soc., 1970, 66, 794-799. [all data]

Wartenberg and Lerner-Steinberg, 1925
Wartenberg, H.; Lerner-Steinberg, Heat of formation of formaldehyde, Z. Angew. Chem., 1925, 38, 591-592. [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]

Thompson, 1941
Thompson, H.W., Thermodynamic functions and equilibria of formaldehyde, deuteroformaldehyde, phosgene and thiophosgene, Trans. Faraday Soc., 1941, 37, 251-260. [all data]

Pillai M.G.K., 1961
Pillai M.G.K., Potential energy constants, rotational distortion constants, and calculated thermodynamic properties for some planar XYZ2 molecules, J. Mol. Spectrosc., 1961, 6, 465-471. [all data]

Gurvich, Veyts, et al., 1989
Gurvich, L.V.; Veyts, I.V.; Alcock, C.B., Thermodynamic Properties of Individual Substances, 4th ed.; Vols. 1 and 2, Hemisphere, New York, 1989. [all data]

Chao J., 1980
Chao J., Perfect gas thermodynamic properties of methanal, ethanal and their deuterated species, Thermochim. Acta, 1980, 41, 41-54. [all data]

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]

Spence and Wild, 1935
Spence, R.; Wild, W., The Vapor Pressure Curve of Formaldehyde and Some Related Data, J. Chem. Soc., 1935, 1935, 506-9. [all data]

Anonymous, 1958
Anonymous, R., , Am. Pet. Inst. Res. Proj. 45, Ohio State Univ., 1958. [all data]

Harries, 1901
Harries, C.D., Chem. Ber., 1901, 34, 635. [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]

Spence and Wild, 1935, 2
Spence, Robert; Wild, William, 114. The vapour-pressure curve of formaldehyde, and some related data, J. Chem. Soc., 1935, 506, https://doi.org/10.1039/jr9350000506 . [all data]

Spence and Wild, 1935, 3
Spence, R.; Wild, W., The Vapour-Pressure Curve of Formaldehyde, and Some Related Data, J. Chem. Soc., 1935, 138, 506-509, https://doi.org/10.1039/jr9350000506 . [all data]

Vasil'ev and Lebedev, 1998
Vasil'ev, V.G.; Lebedev, B.V., Thermodynamic Properties of Aliphatic Aldehydes and Polyaldehydes: Effect of Composition and Structure, Polym. Sci., Ser. A, 1998, 40, 5, 464. [all data]


Notes

Go To: Top, Gas phase thermochemistry data, Phase change data, References