Furan
- Formula: C4H4O
- Molecular weight: 68.0740
- IUPAC Standard InChIKey: YLQBMQCUIZJEEH-UHFFFAOYSA-N
- CAS Registry Number: 110-00-9
- 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: Divinylene oxide; Furfuran; Oxacyclopentadiene; Oxole; Tetrole; Furane; Furfurane; NCI-C56202; Rcra waste number U124; UN 2389; 1,4-Epoxy-1,3-butadiene
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Gas phase thermochemistry data
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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 | -27.7 | kJ/mol | N/A | Zaheeruddin and Lodhi, 1991 | Value computed using ΔfHliquid° value of -55.4 kj/mol from Zaheeruddin and Lodhi, 1991 and ΔvapH° value of 27.6 kj/mol from Guthrie, Scott, et al., 1952.; DRB |
ΔfH°gas | -34.7 | kJ/mol | Ccb | Guthrie, Scott, et al., 1952 | ALS |
ΔfH°gas | -29.8 | kJ/mol | N/A | Landrieu, Baylocq, et al., 1929 | Value computed using ΔfHliquid° value of -57.5 kj/mol from Landrieu, Baylocq, et al., 1929 and ΔvapH° value of 27.6 kj/mol from Guthrie, Scott, et al., 1952.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.26 | 50. | Dorofeeva O.V., 1992 | p=1 bar. Selected entropies and heat capacities are in good agreement with those obtained in other statistical calculations [ Guthrie G.B., 1952, Bak B., 1955, Rico M., 1967, Soptrajanov B., 1968, Chao J., 1986, Klots T.D., 1994].; GT |
33.53 | 100. | ||
36.39 | 150. | ||
43.60 | 200. | ||
59.43 | 273.15 | ||
65.4 ± 1.5 | 298.15 | ||
65.85 | 300. | ||
88.80 | 400. | ||
107.82 | 500. | ||
122.77 | 600. | ||
134.59 | 700. | ||
144.13 | 800. | ||
152.00 | 900. | ||
158.60 | 1000. | ||
164.20 | 1100. | ||
168.97 | 1200. | ||
173.08 | 1300. | ||
176.62 | 1400. | ||
179.69 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
70.29 | 317.25 | Guthrie G.B., 1952 | GT |
80.12 | 358.20 | ||
90.00 | 402.20 | ||
99.58 | 449.20 | ||
106.48 | 487.20 |
Condensed phase thermochemistry data
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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 | Ccb | Zaheeruddin and Lodhi, 1991 | uncertain value: -55.36 kJ/mol; ALS | ||
ΔfH°liquid | -62.34 | kJ/mol | Ccb | Guthrie, Scott, et al., 1952 | ALS |
ΔfH°liquid | -57.45 | kJ/mol | Ccb | Landrieu, Baylocq, et al., 1929 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | Ccb | Zaheeruddin and Lodhi, 1991 | uncertain value: -2090.36 kJ/mol; ALS | ||
ΔcH°liquid | -2083.5 | kJ/mol | Ccb | Guthrie, Scott, et al., 1952 | Corresponding ΔfHºliquid = -62.17 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -2088. | kJ/mol | Ccb | Landrieu, Baylocq, et al., 1929 | Corresponding ΔfHºliquid = -57.3 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 176.65 | J/mol*K | N/A | Guthrie, Scott, et al., 1952, 2 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
114.56 | 298.15 | Guthrie, Scott, et al., 1952, 2 | T = 11 to 300 K.; DH |
Phase change data
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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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 304.7 ± 0.6 | K | AVG | N/A | Average of 12 out of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 187.44 | K | N/A | Guanquan, Ott, et al., 1986 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 187.56 | K | N/A | Goates, Ott, et al., 1973 | Uncertainty assigned by TRC = 0.05 K; TRC |
Tfus | 187.15 | K | N/A | Brooks and Pilcher, 1959 | Uncertainty assigned by TRC = 1. K; TRC |
Tfus | 187.47 | K | N/A | Boord, Greenlee, et al., 1946 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 187.55 | K | N/A | Dolliver, Gresham, et al., 1938 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 187.54 | K | N/A | Wilhoit, Chao, et al., 1985 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 187.55 | K | N/A | Guthrie, Scott, et al., 1952, 3 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 490.2 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 490.2 | K | N/A | Cheng, McCoubrey, et al., 1962 | Uncertainty assigned by TRC = 0.3 K; Visual (5-cm 2-mm bore tubes) in nitrate-nitrite bath, TE or TH cal. vs NPL thermometer.; TRC |
Tc | 487. | K | N/A | Kobe, Ravicz, et al., 1956 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 53.20 | bar | N/A | Kobe, Ravicz, et al., 1956 | Uncertainty assigned by TRC = 1.172 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.219 | l/mol | N/A | Kobe, Ravicz, et al., 1956 | Uncertainty assigned by TRC = 0.005 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 27.71 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 28.2 | kJ/mol | N/A | Moiseev and Antonova, 1970 | Based on data from 277. to 323. K.; AC |
ΔvapH° | 27.6 | kJ/mol | N/A | Guthrie, Scott, et al., 1952 | DRB |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
305.2 | 1.01 | Aldrich Chemical Company Inc., 1990 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
27.1 | 304.5 | N/A | Majer and Svoboda, 1985 | |
27.451 | 298.15 | N/A | Guthrie, Scott, et al., 1952, 2 | P = 79.934 kPa; DH |
30.2 | 253. | A | Stephenson and Malanowski, 1987 | Based on data from 238. to 356. K.; AC |
27.7 | 304.36 | E | Guthrie, Scott, et al., 1952 | ALS |
28.6 | 290. | N/A | Guthrie, Scott, et al., 1952, 2 | Based on data from 275. to 334. K. See also Boublik, Fried, et al., 1984.; AC |
27.2 | 304.2 | V | Mathews and Fehlandt, 1931 | ALS |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
279. to 305. | 42.32 | 0.2802 | 490.2 | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
92.07 | 298.15 | Guthrie, Scott, et al., 1952, 2 | P; DH |
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 |
---|---|---|---|---|---|
275.70 to 334.58 | 4.10003 | 1060.801 | -45.416 | Guthrie, Scott, et al., 1952, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.8 | 187.6 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
13.64 | 150.0 | Domalski and Hearing, 1996 | CAL |
20.29 | 187.6 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
2.0468 | 150.0 | crystaline, II | crystaline, I | Guthrie, Scott, et al., 1952, 2 | DH |
3.8024 | 187.55 | crystaline, I | liquid | Guthrie, Scott, et al., 1952, 2 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
13.65 | 150.0 | crystaline, II | crystaline, I | Guthrie, Scott, et al., 1952, 2 | DH |
20.27 | 187.55 | crystaline, I | liquid | Guthrie, Scott, et al., 1952, 2 | DH |
Reaction thermochemistry data
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
RCD - Robert C. Dunbar
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: C4H5O+ + C4H4O = (C4H5O+ • C4H4O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 42. | kJ/mol | PHPMS | Hiraoka, Takimoto, et al., 1987 | gas phase; ΔrH<; M |
ΔrH° | 79. | kJ/mol | PHPMS | Meot-Ner (Mautner), Ross, et al., 1985 | gas phase; Entropy change calculated or estimated, ΔrH<; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | N/A | Meot-Ner (Mautner), Ross, et al., 1985 | gas phase; Entropy change calculated or estimated, ΔrH<; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
28. | 382. | PHPMS | Meot-Ner (Mautner), Ross, et al., 1985 | gas phase; Entropy change calculated or estimated, ΔrH<; M |
C4H3O- + =
By formula: C4H3O- + H+ = C4H4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1636.2 ± 1.5 | kJ/mol | G+TS | Grabowski and Owusu | gas phase; B |
ΔrH° | 1624. ± 13. | kJ/mol | G+TS | DePuy, Kass, et al., 1988 | gas phase; Order:H2O < furan < 2-Me-furan < MeOH. D exchange indicates anion at C-2.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1602.1 ± 0.84 | kJ/mol | IMRE | Grabowski and Owusu | gas phase; B |
ΔrG° | 1590. ± 13. | kJ/mol | IMRB | DePuy, Kass, et al., 1988 | gas phase; Order:H2O < furan < 2-Me-furan < MeOH. D exchange indicates anion at C-2.; B |
By formula: C4H4O + 2H2 = C4H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -151.1 ± 0.50 | kJ/mol | Chyd | Dolliver, Gresham, et al., 1938, 2 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -153.3 ± 0.50 kJ/mol; At 355 °K; ALS |
By formula: C4H4O+ + C4H4O = (C4H4O+ • C4H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 72.0 | kJ/mol | PHPMS | Hiraoka, Takimoto, et al., 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 99.2 | J/mol*K | PHPMS | Hiraoka, Takimoto, et al., 1987 | gas phase; M |
By formula: (C4H4O+ • C4H4O) + C4H4O = (C4H4O+ • 2C4H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 30. | kJ/mol | PHPMS | Hiraoka, Takimoto, et al., 1987 | gas phase; ΔrH<; M |
By formula: Na+ + C4H4O = (Na+ • C4H4O)
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
49.0 | 298. | IMRE | McMahon and Ohanessian, 2000 | Anchor alanine=39.89; RCD |
Henry's Law data
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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 |
---|---|---|---|---|
0.18 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. |
IR Spectrum
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Coblentz Society, Inc.
Gas Phase Spectrum
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Notice: Except where noted, spectra from this collection were measured on dispersive instruments, often in carefully selected solvents, and hence may differ in detail from measurements on FTIR instruments or in other chemical environments. More information on the manner in which spectra in this collection were collected can be found here.
Notice: Concentration information is not available for this spectrum and, therefore, molar absorptivity values cannot be derived.
Additional Data
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Owner | Copyright (C) 1987 by the Coblentz Society Collection (C) 2018 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | DOW CHEMICAL COMPANY |
Source reference | COBLENTZ NO. 8800 |
Date | 1964 |
State | GAS (100 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg) |
Instrument | DOW KBr FOREPRISM-GRATING |
Instrument parameters | GRATING CHANGED AT 5.0, 7.5, 15.0 MICRON |
Path length | 5 CM |
Resolution | 2 |
Sampling procedure | TRANSMISSION |
Data processing | DIGITIZED BY COBLENTZ SOCIETY (BATCH II) FROM HARD COPY |
Mass spectrum (electron ionization)
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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Due to licensing restrictions, this spectrum cannot be downloaded.
Owner | NIST Mass Spectrometry Data Center Collection (C) 2014 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | Japan AIST/NIMC Database- Spectrum MS-NW- 16 |
NIST MS number | 228308 |
UV/Visible spectrum
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Spectrum
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Additional Data
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Source | Mason, 1967 |
---|---|
Owner | INEP CP RAS, NIST OSRD Collection (C) 2007 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
Origin | INSTITUTE OF ENERGY PROBLEMS OF CHEMICAL PHYSICS, RAS |
Source reference | RAS UV No. 19848 |
Instrument | Hilger Uvispek |
Boiling point | 32 |
Vibrational and/or electronic energy levels
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Takehiko Shimanouchi
Symmetry: C2ν Symmetry Number σ = 2
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a1 | 1 | CH str | 3154 | D | 3154 VS p | liq. | ||||
a1 | 2 | CH str | 3140 | D | 3140 sh | gas | ||||
a1 | 3 | ip-Ring II | 1491 | C | 1491 VS | gas | 1483 VS p | liq. | ||
a1 | 4 | ip-Ring III | 1384 | C | 1384 M | gas | 1380 S p | liq. | ||
a1 | 5 | ip-Ring IV | 1140 | D | 1140 sh | liq. | 1137 VS p | liq. | ||
a1 | 6 | CH ip-bend | 1066 | C | 1066 S | gas | 1061 M p | liq. | ||
a1 | 7 | CH ip-bend | 995 | C | 995 VS | gas | 986 M p | liq. | ||
a1 | 8 | ip-Ring VII | 871 | C | 871 S | gas | ||||
a2 | 9 | CH op-bend | 863 | C | ia | OC(ν9+ν16, ν9+ν17, ν9+ν19, ν9+ν2) | ||||
a2 | 10 | CH op-bend | 728 | D | ia | 728 W dp | liq. | |||
a2 | 11 | op-Ring I | 613 | D | ia | 613 VW dp | liq. | |||
b1 | 12 | CH str | 3161 | C | 3161 M | gas | ||||
b1 | 13 | CH str | 3129 | C | 3129 M | gas | 3121 S dp | liq. | ||
b1 | 14 | ip-Ring I | 1556 | C | 1556 W | gas | ||||
b1 | 15 | CH ip-bend | 1267 | C | 1267 VW | gas | 1270 VW dp | liq. | ||
b1 | 16 | CH ip-bend | 1180 | C | 1180 VS | gas | 1171 W dp | liq. | ||
b1 | 17 | ip-Ring V | 1040 | D | 1040 sh | liq. | 1034 M dp | liq. | ||
b1 | 18 | ip-Ring VI | 873 | D | 873 W dp | liq. | ||||
b2 | 19 | CH op-bend | 838 | C | 838 VW | gas | 839 W dp | liq. | ||
b2 | 20 | CH op-bend | 745 | C | 745 VS | gas | ||||
b2 | 21 | op-Ring II | 603 | C | 603 S | gas | 601 W dp | liq. | ||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
ia | Inactive |
sh | Shoulder |
p | Polarized |
dp | Depolarized |
OC | Frequency estimated from an overtone or a combination tone indicated in the parentheses. |
C | 3~6 cm-1 uncertainty |
D | 6~15 cm-1 uncertainty |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Zaheeruddin and Lodhi, 1991
Zaheeruddin, M.; Lodhi, Z.H.,
Enthalpies of formation of some cyclic compounds,
Phys. Chem. (Peshawar Pak.), 1991, 10, 111-118. [all data]
Guthrie, Scott, et al., 1952
Guthrie, G.B., Jr.; Scott, D.W.; Hubbard, W.N.; Katz, C.; McCullough, J.P.; Gross, M.E.; Williamson, K.D.; Waddington, G.,
Thermodynamic properties of furan,
J. Am. Chem. Soc., 1952, 74, 4662-46. [all data]
Landrieu, Baylocq, et al., 1929
Landrieu, P.; Baylocq, F.; Johnson, J.R.,
Etude thermochimique dans la serie furanique,
Bull. Soc. Chim. France, 1929, 45, 36-49. [all data]
Dorofeeva O.V., 1992
Dorofeeva O.V.,
Ideal gas thermodynamic properties of oxygen heterocyclic compounds. Part 1. Three-membered, four-membered and five-membered rings,
Thermochim. Acta, 1992, 194, 9-46. [all data]
Guthrie G.B., 1952
Guthrie G.B., Jr.,
Thermodynamic properties of furan,
J. Am. Chem. Soc., 1952, 74, 4662-4669. [all data]
Bak B., 1955
Bak B.,
Infrared absorption spectra of alpha and beta monodeutero, and alpha, alpha' dideutero furan vapors. Heat capacity and entropy of furan,
Acta Chem. Scand., 1955, 9, 749-762. [all data]
Rico M., 1967
Rico M.,
Fundamental vibrations of furan and deuterated derivatives,
J. Mol. Spectrosc., 1967, 24, 133-148. [all data]
Soptrajanov B., 1968
Soptrajanov B.,
Thermodynamic functions of furan and deuterated furans,
Croat. Chem. Acta, 1968, 40, 241-245. [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]
Klots T.D., 1994
Klots T.D.,
Complete vapor phase assignment for the fundamental vibrations of furan, pyrrole and thiophene,
Spectrochim. Acta, 1994, A50, 765-795. [all data]
Guthrie, Scott, et al., 1952, 2
Guthrie, G.B., Jr.; Scott, D.W.; Hubbard, W.N.; Katz, C.; McCullough, J.P.; Gross, M.E.; Williamson, K.D.; Waddington, G.,
Thermodynamic properties of furan,
J. Am. Chem. Soc., 1952, 74, 4662-4669. [all data]
Guanquan, Ott, et al., 1986
Guanquan, C.; Ott, J.B.; Goates, J.R.,
(Solid + liquid) Phase Equilibria and Solid-Compound Formation in Tetrachloromethane + furan, + Pyridine, and + N-methylpyrrole,
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°liquid Entropy of liquid at standard conditions T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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