Aniline
- Formula: C6H7N
- Molecular weight: 93.1265
- IUPAC Standard InChIKey: PAYRUJLWNCNPSJ-UHFFFAOYSA-N
- CAS Registry Number: 62-53-3
- 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. - Isotopologues:
- Other names: Benzenamine; Aminobenzene; Aminophen; Anyvim; Benzene, amino-; Blue Oil; C.I. 76000; Phenylamine; Aniline Oil; Aniline reagent; Anilin; Anilina; Benzidam; C.I. Oxidation base 1; Cyanol; Huile D'aniline; Krystallin; Kyanol; NCI-C03736; Rcra waste number U012; UN 1547; Benzeneamine
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | 20.80 ± 0.21 | kcal/mol | Ccb | Hatton, Hildenbrand, et al., 1962 | ALS |
ΔfH°gas | 19.7 | kcal/mol | Ccb | Vriens and Hill, 1952 | ALS |
ΔfH°gas | 19.9 | kcal/mol | N/A | Cole and Gilbert, 1951 | Value computed using ΔfHliquid° value of 30.8 kj/mol from Cole and Gilbert, 1951 and ΔvapH° value of 52.4 kj/mol from Vriens and Hill, 1952.; DRB |
ΔfH°gas | 19.3 ± 0.6 | kcal/mol | Ccb | Anderson and Gilbert, 1942 | %hf calculated possible error by author; ALS |
ΔfH°gas | 20.4 | kcal/mol | N/A | Lemoult, 1907 | Value computed using ΔfHliquid° value of 33.0 kj/mol from Lemoult, 1907 and ΔvapH° value of 52.4 kj/mol from Vriens and Hill, 1952.; DRB |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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 | 7.47 ± 0.20 | kcal/mol | Ccb | Hatton, Hildenbrand, et al., 1962 | ALS |
ΔfH°liquid | 7.1 | kcal/mol | Ccb | Vriens and Hill, 1952 | ALS |
ΔfH°liquid | 7.37 | kcal/mol | Cm | Cole and Gilbert, 1951 | ALS |
ΔfH°liquid | 8.0 | kcal/mol | Ccb | Lemoult, 1907 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -810.96 ± 0.24 | kcal/mol | Ccb | Hatton, Hildenbrand, et al., 1962 | ALS |
ΔcH°liquid | -810.7 | kcal/mol | Ccb | Vriens and Hill, 1952 | ALS |
ΔcH°liquid | -810.79 | kcal/mol | Cm | Cole and Gilbert, 1951 | ALS |
ΔcH°liquid | -810.6 ± 3.0 | kcal/mol | Ccb | Anderson and Gilbert, 1942 | %hf calculated possible error by author; ALS |
ΔcH°liquid | -815.3 | kcal/mol | Ccb | Lemoult, 1907 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 45.722 | cal/mol*K | N/A | Hatton, Hildenbrand, et al., 1962 | DH |
S°liquid | 45.79 | cal/mol*K | N/A | Parks, Huffman, et al., 1933 | Extrapolation below 90 K, 45.27 J/mol*K.; DH |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°solid | -810.4 | kcal/mol | Ccb | Willis, 1947 | ALS |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
46.39 | 298. | Lesbats and Lichanot, 1987 | T = 200 to 300 K.; DH |
45.652 | 298.15 | Nichols and Wads, 1975 | DH |
46.30 | 298. | Deshpande and Bhatagadde, 1971 | T = 298 to 318 K.; DH |
45.901 | 298.15 | Hatton, Hildenbrand, et al., 1962 | T = 15 to 300 K. Cp(liq, cal/mol·K) = 33.71 + 0.0409T (15 to 300 K).; DH |
45.89 | 293. | Crtzen, Jost, et al., 1957 | DH |
47.20 | 323. | Hough, Mason, et al., 1950 | T = 323 to 453 K.; DH |
26.099 | 267.3 | Ziegler and Andrews, 1942 | T = 40.84 K.; DH |
43.91 | 288. | Radulescu and Jula, 1934 | DH |
42.73 | 298.15 | Ferguson and Miller, 1933 | T = 293 to 323 K. Data calculated from equation.; DH |
45.631 | 298.2 | Parks, Huffman, et al., 1933 | T = 94 to 298 K. Value is unsmoothed experimental datum.; DH |
46.219 | 298.2 | Lang, 1928 | T = 5 to 60°C.; DH |
46.01 | 298. | von Reis, 1881 | T = 290 to 465 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, IR Spectrum, 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 457. ± 2. | K | AVG | N/A | Average of 46 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 267.0 ± 0.3 | K | AVG | N/A | Average of 19 out of 24 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 267.13 | K | N/A | Hatton, Hildenbrand, et al., 1962, 2 | Uncertainty assigned by TRC = 0.02 K; from plot of 1/f vs T; TRC |
Ttriple | 267.300 | K | N/A | Ziegler and Andrews, 1942, 2 | Uncertainty assigned by TRC = 0.2 K; TRC |
Ttriple | 266.9 | K | N/A | Parks, Huffman, et al., 1933, 2 | Uncertainty assigned by TRC = 0.1 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 698.8 ± 0.4 | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 52.4 ± 0.2 | atm | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.48 | mol/l | N/A | Lagutkin and Kuropatkin, 1981 | Uncertainty assigned by TRC = 0.05 mol/l; calculated from corr. Zc, and lit. values of Tc and Pc; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Zc | 0.26 | none | N/A | Lagutkin and Kuropatkin, 1981 | Uncertainty assigned by TRC = 0.003 none; Correlation based on literature values of 2nd vireal coeff.; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 13. ± 1. | kcal/mol | AVG | N/A | Average of 7 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
12.2 ± 0.05 | 360. | EB | Steele, Chirico, et al., 2002 | Based on data from 350. to 499. K.; AC |
11.5 ± 0.05 | 400. | EB | Steele, Chirico, et al., 2002 | Based on data from 350. to 499. K.; AC |
10.8 ± 0.05 | 440. | EB | Steele, Chirico, et al., 2002 | Based on data from 350. to 499. K.; AC |
10.1 ± 0.1 | 480. | EB | Steele, Chirico, et al., 2002 | Based on data from 350. to 499. K.; AC |
10.9 | 444. | N/A | Lee, Chen, et al., 1992 | Based on data from 421. to 591. K.; AC |
12.5 | 288. | A | Stephenson and Malanowski, 1987 | Based on data from 273. to 338. K.; AC |
12.8 | 319. | A | Stephenson and Malanowski, 1987 | Based on data from 304. to 485. K.; AC |
11.6 | 388. | A | Stephenson and Malanowski, 1987 | Based on data from 373. to 458. K.; AC |
11.1 | 470. | A | Stephenson and Malanowski, 1987 | Based on data from 455. to 523. K.; AC |
10.14 | 457.2 | N/A | Majer and Svoboda, 1985 | |
12.3 | 350. | N/A | Maher and Smith, 1979 | Based on data from 313. to 386. K.; AC |
12.6 | 293. | N/A | Ravdel and Danilov, 1968 | Based on data from 288. to 298. K.; AC |
12.9 | 319. | N/A | Hatton, Hildenbrand, et al., 1962 | Based on data from 304. to 457. K.; AC |
12.7 | 333. | C | Hatton, Hildenbrand, et al., 1962 | AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kcal/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 333. | 19.28 | 0.3744 | 699. | Majer 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 |
---|---|---|---|---|---|
304. to 457. | 4.33970 | 1661.858 | -74.048 | Hatton, Hildenbrand, et al., 1962 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.5189 | 267.13 | Hatton, Hildenbrand, et al., 1962 | DH |
2.519 | 267.1 | Ahmed and Eades, 1972 | See also Domalski and Hearing, 1996.; AC |
2.610 | 267.3 | Ziegler and Andrews, 1942 | AC |
2.5229 | 266.8 | Parks, Huffman, et al., 1933 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.457 | 266.8 | Parks, Huffman, et al., 1933 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, IR Spectrum, 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
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: Br- + C6H7N = (Br- • C6H7N)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.6 ± 1.8 | kcal/mol | IMRE | Paul and Kebarle, 1991 | gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | N/A | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 6.1 ± 1.0 | kcal/mol | IMRE | Paul and Kebarle, 1991 | gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
6.1 | 423. | PHPMS | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
C6H6N- + =
By formula: C6H6N- + H+ = C6H7N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 368.18 ± 0.30 | kcal/mol | D-EA | Wren, Vogelhuber, et al., 2012 | gas phase; B |
ΔrH° | 366.4 ± 2.1 | kcal/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 360.91 ± 0.67 | kcal/mol | H-TS | Wren, Vogelhuber, et al., 2012 | gas phase; B |
ΔrG° | 359.1 ± 2.0 | kcal/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
By formula: C9H13N+ + C6H7N = (C9H13N+ • C6H7N)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.3 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | (26.) | cal/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
5.9 | 283. | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: C7H9N+ + C6H7N = (C7H9N+ • C6H7N)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.7 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26. | cal/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 9.0 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: C8H11N+ + C6H7N = (C8H11N+ • C6H7N)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.2 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26. | cal/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 6.5 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: F- + C6H7N = (F- • C6H7N)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 31.2 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26.2 | cal/mol*K | N/A | Larson and McMahon, 1983 | gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 23.4 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; B,M |
By formula: C6H7N+ + C6H7N = (C6H7N+ • C6H7N)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17.5 | kcal/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.6 | cal/mol*K | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
By formula: C6H7N + C8H4O3 = C14H11NO3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -12.8 | kcal/mol | Kin | Kalnin'sh, 1988 | liquid phase; solvent: Acetonitrile; ALS |
ΔrH° | -13.0 | kcal/mol | Kin | Pravednikov, Kardash, et al., 1973 | solid phase; solvent: Tetrahydrofuran; ALS |
By formula: C7H9N = 0.5C8H11N + 0.5C6H7N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -0.8 | kcal/mol | Eqk | Matvienko, Kachurin, et al., 1982 | liquid phase; Methansulfonic acid; ALS |
ΔrH° | -0.9 | kcal/mol | Kin | Kachurin, Matvienko, et al., 1979 | liquid phase; ALS |
By formula: K+ + C6H7N = (K+ • C6H7N)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.8 | kcal/mol | HPMS | Davidson and Kebarle, 1976 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 23.7 | cal/mol*K | HPMS | Davidson and Kebarle, 1976 | gas phase; M |
By formula: C7H5IO + C6H7N = HI + C13H11NO
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -39.7 ± 0.5 | kcal/mol | Cac | Kiselev, Khuzyasheva, et al., 1979 | liquid phase; solvent: Benzene; ALS |
By formula: C7H5BrO + C6H7N = HBr + C13H11NO
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -38.6 ± 0.2 | kcal/mol | Cac | Kiselev, Khuzyasheva, et al., 1979 | liquid phase; solvent: Benzene; ALS |
By formula: C6H7N + C7H5ClO = HCl + C13H11NO
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -35.6 ± 0.2 | kcal/mol | Cac | Kiselev, Khuzyasheva, et al., 1979 | liquid phase; solvent: Benzene; ALS |
By formula: C8H9NO + H2O = C6H7N + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -10.05 ± 0.06 | kcal/mol | Cm | Wadso, 1965 | solid phase; Heat of hydrolysis; ALS |
By formula: C7H4N2O3 + C6H7N = C13H11N3O3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -20.0 ± 0.07 | kcal/mol | Cm | Kiselev, Malkov, et al., 1989 | liquid phase; solvent: Dioxane; #TDE; ALS |
By formula: C7H11NO + C6H7N = C13H18N2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -23.5 ± 0.26 | kcal/mol | Cm | Kiselev, Malkov, et al., 1989 | liquid phase; solvent: Dioxane; ALS |
By formula: C15H17NO2 = C9H10O2 + C6H7N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27.1 ± 0.5 | kcal/mol | Cm | Kuznetsova, Rakova, et al., 1975 | solid phase; solvent: DMF; ALS |
By formula: C7H5NO + C6H7N = C13H12N2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -19.7 ± 0.48 | kcal/mol | Cm | Kiselev, Malkov, et al., 1989 | liquid phase; solvent: Dioxane; ALS |
By formula: C13H12N2O = C7H5NO + C6H7N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 43.4 ± 1.0 | kcal/mol | Eqk | Chimishkyan, Svetlova, et al., 1984 | solid phase; Dissociation; ALS |
By formula: I- + C6H7N = (I- • C6H7N)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12.9 ± 1.0 | kcal/mol | TDAs | Caldwell, Masucci, et al., 1989 | gas phase; B,M |
By formula: C4H5N3O + C6H7N = C8H9NO + C2H3N3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -17.28 ± 0.08 | kcal/mol | Cm | Wadso, 1962 | solid phase; ALS |
By formula: C3H4N4O + C6H7N = C8H9NO + CH2N4
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -20.22 ± 0.08 | kcal/mol | Cm | Wadso, 1962 | solid phase; ALS |
By formula: C4H6O3 + C6H7N = C8H9NO + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -24.11 ± 0.06 | kcal/mol | Cm | Wadso, 1962 | liquid phase; ALS |
By formula: C7H5NO + C6H7N = C13H12N2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -21.3 ± 1.2 | kcal/mol | Cm | Pannone and Macosko, 1987 | liquid phase; ALS |
IR Spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, References, Notes
Data compiled by: Coblentz Society, Inc.
- LIQUID (NEAT); BECKMAN IR-7 (GRATING); DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 cm-1 resolution
- SOLUTION (10% IN CCl4 FOR 3800-1300, 10% IN CS2 FOR 1300-650, 10% IN CCl4 FOR 650-250 CM-1) VERSUS SOLVENT; PERKIN-ELMER 521 (GRATING); DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 cm-1 resolution
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Hatton, Hildenbrand, et al., 1962
Hatton, W.E.; Hildenbrand, D.L.; Sinke, G.C.; Stull, D.R.,
Chemical thermodynamic properties of aniline,
J. Chem. Eng. Data, 1962, 7, 229-231. [all data]
Vriens and Hill, 1952
Vriens, G.N.; Hill, A.G.,
Equilibria of several reactions of aromatic amines,
Ind. Eng. Chem., 1952, 44, 2732-27. [all data]
Cole and Gilbert, 1951
Cole, L.G.; Gilbert, E.C.,
The heats of combustion of some nitrogen compounds and the apparent energy of the N-N bond,
J. Am. Chem. Soc., 1951, 73, 5423-5427. [all data]
Anderson and Gilbert, 1942
Anderson, C.M.; Gilbert, E.C.,
The apparent energy of the N-N bond as calculated from heats of combustion,
J. Am. Chem. Soc., 1942, 64, 2369-2372. [all data]
Lemoult, 1907
Lemoult, M.P.,
Recherches theoriques et experimentales sur les chaleurs de combustion et de formation des composes organiques,
Ann. Chim. Phys., 1907, 12, 395-432. [all data]
Parks, Huffman, et al., 1933
Parks, G.S.; Huffman, H.M.; Barmore, M.,
Thermal data on organic compounds. XI. The heat capacities,
entropies and free energies of ten compounds containing oxygen or nitrogen. J. Am. Chem. Soc., 1933, 55, 2733-2740. [all data]
Willis, 1947
Willis, J.B.,
The heats of combustion of some organic bases and their salts. The resonance energies of acridine and phenazine,
Trans. Faraday Soc., 1947, 43, 97-102. [all data]
Lesbats and Lichanot, 1987
Lesbats, C.; Lichanot, A.,
Capacites calorifiques de durcisseurs amines et resines epoxydes,
Thermochim. Acta, 1987, 109, 317-329. [all data]
Nichols and Wads, 1975
Nichols, N.; Wads, I.,
Thermochemistry of solutions of biochemical model compounds. 3. Some benzene derivatives in aqueous solution,
J. Chem. Thermodynam., 1975, 7, 329-336. [all data]
Deshpande and Bhatagadde, 1971
Deshpande, D.D.; Bhatagadde, L.G.,
Heat capacities at constant volume, free volumes, and rotational freedom in some liquids,
Aust. J. Chem., 1971, 24, 1817-1822. [all data]
Crtzen, Jost, et al., 1957
Crtzen, J.L.; Jost, W.; Sieg, L.,
Gleichgewichtsmessungen im System Anilin-N-Methylanilin, N-N-Dimethylanilin, 1,2-Äthandiol,
Z. Elektrochem., 1957, 61, 230-246. [all data]
Hough, Mason, et al., 1950
Hough, E.W.; Mason, D.M.; Sage, B.H.,
Heat capacities of several organic liquids,
J. Am. Chem. Soc., 1950, 72, 5775-5777. [all data]
Ziegler and Andrews, 1942
Ziegler, W.T.; Andrews, D.H.,
The heat capacity of benzene-d6,
J. Am. Chem. Soc., 1942, 64, 2482-2485. [all data]
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Radulescu, D.; Jula, O.,
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Notes
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- Symbols used in this document:
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 Zc Critical compressability factor ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔcH°solid Enthalpy of combustion of solid 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 ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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