Heptane
- Formula: C7H16
- Molecular weight: 100.2019
- IUPAC Standard InChIKey: IMNFDUFMRHMDMM-UHFFFAOYSA-N
- CAS Registry Number: 142-82-5
- 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: n-Heptane; Dipropylmethane; Heptyl hydride; Skellysolve C; n-C7H16; Eptani; Heptan; Heptanen; Gettysolve-C; NSC 62784
- Permanent link for this species. Use this link for bookmarking this species for future reference.
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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 |
---|---|---|---|---|---|
ΔfH°gas | -187.8 ± 0.79 | kJ/mol | Ccb | Prosen and Rossini, 1945 | ALS |
ΔfH°gas | -189.3 | kJ/mol | N/A | Davies and Gilbert, 1941 | Value computed using ΔfHliquid° value of -225.9±1.3 kj/mol from Davies and Gilbert, 1941 and ΔvapH° value of 36.6 kj/mol from Prosen and Rossini, 1945.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
127.65 | 200. | Scott D.W., 1974 | Recommended values were obtained from the consistent correlation scheme for alkanes [ Scott D.W., 1974, 2, Scott D.W., 1974]. This approach gives a better agreement with experimental data than the statistical thermodynamics calculation [ Pitzer K.S., 1944, Pitzer K.S., 1946].; GT |
154.64 | 273.15 | ||
165.2 ± 0.3 | 298.15 | ||
165.98 | 300. | ||
210.66 | 400. | ||
252.09 | 500. | ||
287.44 | 600. | ||
317.15 | 700. | ||
342.25 | 800. | ||
363.59 | 900. | ||
381.58 | 1000. | ||
397.06 | 1100. | ||
410.45 | 1200. | ||
422.58 | 1300. | ||
435.14 | 1400. | ||
443.50 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
191.50 ± 0.19 | 357.10 | Waddington G., 1947 | GT |
198.78 ± 0.20 | 373.15 | ||
210.75 ± 0.21 | 400.40 | ||
225.31 ± 0.23 | 434.35 | ||
238.49 ± 0.24 | 466.10 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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 | -224.4 ± 0.79 | kJ/mol | Ccb | Prosen and Rossini, 1945 | ALS |
ΔfH°liquid | -225.9 ± 1.3 | kJ/mol | Ccb | Davies and Gilbert, 1941 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -4817. ± 8. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 328.57 | J/mol*K | N/A | Huffman, Gross, et al., 1961 | DH |
S°liquid | 327.98 | J/mol*K | N/A | Douglas, Furukawa, et al., 1954 | DH |
S°liquid | 328.86 | J/mol*K | N/A | Pitzer K.S., 1940 | DH |
S°liquid | 330.1 | J/mol*K | N/A | Huffman, Parks, et al., 1930 | Extrapolation below 90 K, 71.00 J/mol*K. Based on previously published specific heat data, 30PAR/HUF.; DH |
S°liquid | 326.4 | J/mol*K | N/A | Parks, Huffman, et al., 1930 | Extrapolation below 90 K, 71.00 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
224.64 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
224.72 | 298.15 | Saito and Tanaka, 1988 | DH |
224.73 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
222.88 | 293.15 | Kalali, Kohler, et al., 1987 | T = 293.15, 313.15 K.; DH |
224.721 | 298.15 | Tanaka, 1987 | DH |
225.14 | 300. | Van Miltenburg, Van den Berg, et al., 1987 | T = 10 to 350 K.; DH |
224.71 | 298.15 | Wilhelm, Inglese, et al., 1987 | DH |
224.781 | 298.15 | Baluja, Bravo, et al., 1985 | DH |
224.781 | 298.15 | Lainez, Rodrigo, et al., 1985 | DH |
224.731 | 298.15 | Tanaka, Nakamichi, et al., 1985 | DH |
224.71 | 298.15 | Grolier, Inglese, et al., 1984 | DH |
224.78 | 298.15 | Roux, Grolier, et al., 1984 | DH |
224.764 | 298.15 | Kimura, Treszczanowicz, et al., 1983 | DH |
225.33 | 300. | Tan, Zhou, et al., 1983 | T = 220 to 380 K.; DH |
224.8 | 298.15 | Tanaka, 1982 | DH |
224.0 | 298. | Zaripov, 1982 | T = 298, 323, 363 K.; DH |
224.69 | 298.15 | Grolier, Inglese, et al., 1981 | DH |
224.62 | 297.860 | Kalinowska, Jedlinska, et al., 1980 | T = 185 to 300 K. Unsmoothed experimental datum.; DH |
224.66 | 298.15 | Brown and Ziegler, 1979 | T = 183 to 302 K. Results as equation only.; DH |
225.6 | 300. | Czarnota, 1979 | DH |
224.6 | 298.15 | Grolier, Hamedi, et al., 1979 | DH |
220.00 | 285. | Schaake, Offringa, et al., 1979 | T = 90 to 285 K.; DH |
226.5 | 333.15 | Woycicka and Kalinowska, 1978 | DH |
255.0 | 298.15 | Meijer, Blok, et al., 1977 | T = 160 to 350 K.; DH |
224.707 | 298.15 | Fortier and Benson, 1976 | DH |
223.4 | 298. | Grigor'ev, Rastorguev, et al., 1975 | T = 300 to 463 K.; DH |
224.19 | 298.15 | Holzhauer and Ziegler, 1975 | T = 182 to 312 K. Cp = 866.18820 - 9.9628490T + 0.054561085T2 - 0.00013079634T3 + 1.1957392x10-7T4 J/mol*K.; DH |
226.53 | 303.15 | Woycicka and Kalinowska, 1975 | DH |
225.3 | 298.15 | Diaz pena and Renuncio, 1974 | T = 298 to 323 K.; DH |
226.53 | 298.15 | Kalinowska and Woycicka, 1973 | DH |
209.6 | 250. | Van Miltenburg, 1972 | T = 130 to 263 K.; DH |
328.61 | 298.15 | Oetting F.L., 1963 | DH |
224.93 | 298.15 | Huffman, Gross, et al., 1961 | T = 10 to 300 K.; DH |
224.93 | 298.15 | McCullough and Messerly, 1961 | T = 10 to 370 K. Csat(liq) = 56.582 - 0.14490T + 5.7813x10-4T2 - 4.1667x10-7T3 cal/mol*K.; DH |
247.3 | 332. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 22 to 96 C.; DH |
233.13 | 299.8 | Helfrey, Heiser, et al., 1955 | T = 70 to 220 F.; DH |
224.74 | 298.15 | Douglas, Furukawa, et al., 1954 | T = 20 to 520 K.; DH |
224.74 | 298.15 | Ginnings and Furukawa, 1953 | T = 25 to 520 K.; DH |
224.85 | 298.15 | Osborne and Ginnings, 1947 | T = 278 to 318 K.; DH |
224.60 | 296.5 | Pitzer K.S., 1940 | T = 15 to 318 K. Value is unsmoothed experimental datum.; DH |
211.3 | 298. | Bykov, 1939 | DH |
210.9 | 300.8 | Phillip, 1939 | DH |
223.0 | 298. | Vold, 1937 | Cp given as 0.532 cal/g*K.; DH |
224.3 | 298.1 | Richards and Wallace, 1932 | T = 293 to 323 K.; DH |
222.2 | 299.2 | Parks, Huffman, et al., 1930 | T = 90 to 300 K. Value is unsmoothed experimental datum.; DH |
217.0 | 303. | Willams and Daniels, 1924 | T = 303 to 350 K. Equation only.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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 |
---|---|---|---|---|---|
Tboil | 371.5 ± 0.3 | K | AVG | N/A | Average of 215 out of 227 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 182.6 ± 0.4 | K | AVG | N/A | Average of 51 out of 52 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 182.56 ± 0.03 | K | AVG | N/A | Average of 26 out of 31 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 540. ± 2. | K | AVG | N/A | Average of 27 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 27.4 ± 0.3 | bar | AVG | N/A | Average of 18 out of 19 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.428 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Vc | 0.425 | l/mol | N/A | Zawisza and Vejrosta, 1982 | Uncertainty assigned by TRC = 0.001 l/mol; Visual; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.35 ± 0.07 | mol/l | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 36. ± 3. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
31.77 | 371.6 | N/A | Majer and Svoboda, 1985 | |
34.7 | 345. | N/A | Segura, Wisniak, et al., 2002 | Based on data from 330. to 371. K.; AC |
35.2 | 343. | N/A | Ortega, González, et al., 2001 | Based on data from 328. to 393. K.; AC |
36.1 | 312. | A | Stephenson and Malanowski, 1987 | Based on data from 297. to 375. K. See also Forziati, Norris, et al., 1949.; AC |
36.1 | 313. | N/A | Michou-Saucet, Jose, et al., 1984 | Based on data from 298. to 338. K.; AC |
36.1 | 313. | N/A | Sipowska and Wieczorek, 1984 | Based on data from 298. to 363. K.; AC |
35.6 ± 0.1 | 313. | C | Majer, Svoboda, et al., 1979 | AC |
34.4 ± 0.1 | 333. | C | Majer, Svoboda, et al., 1979 | AC |
33.1 ± 0.1 | 353. | C | Majer, Svoboda, et al., 1979 | AC |
36.4 | 303. | N/A | Van Ness, Soczek, et al., 1967 | Based on data from 288. to 348. K.; AC |
34.5 ± 0.1 | 331. | C | Waddington, Todd, et al., 1947 | AC |
33.2 ± 0.1 | 350. | C | Waddington, Todd, et al., 1947 | AC |
35.4 | 328. | N/A | Thomson, 1946 | Based on data from 313. to 398. K.; AC |
36.0 | 314. | MM | Willingham, Taylor, et al., 1945 | Based on data from 299. to 372. K.; AC |
32.0 | 371. | C | Pitzer K.S., 1940 | AC |
35.5 | 325. | EB | Smith, 1940 | Based on data from 310. to 397. K.; AC |
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 |
---|---|---|---|---|---|
298. to 363. | 53.66 | 0.2831 | 540.2 | Majer 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 |
---|---|---|---|---|---|
185.29 to 295.60 | 4.81803 | 1635.409 | -27.338 | Carruth and Kobayashi, 1973 | Coefficents calculated by NIST from author's data. |
299.07 to 372.43 | 4.02832 | 1268.636 | -56.199 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
57.9 | 183. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
13.990 | 182.57 | Van Miltenburg, Van den Berg, et al., 1987 | DH |
14.053 | 182.59 | Schaake, Offringa, et al., 1979 | DH |
14.037 | 182.55 | Huffman, Gross, et al., 1961 | DH |
14.037 | 182.55 | McCullough and Messerly, 1961 | DH |
14.022 | 182.56 | Douglas, Furukawa, et al., 1954 | DH |
14.022 | 182.56 | Ginnings and Furukawa, 1953 | DH |
14.0407 | 182.52 | Pitzer K.S., 1940 | DH |
14.059 | 182.7 | Meijer, Blok, et al., 1977 | DH |
14.061 | 182.56 | Van Miltenburg, 1972 | DH |
14.0306 | 182.56 | Oetting F.L., 1963 | DH |
14.04 | 182.6 | Domalski and Hearing, 1996 | AC |
14.163 | 182.2 | Huffman, Parks, et al., 1930 | DH |
14.163 | 182.2 | Parks, Huffman, et al., 1930 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
76.96 | 182.59 | Schaake, Offringa, et al., 1979 | DH |
76.89 | 182.55 | Huffman, Gross, et al., 1961 | DH |
76.89 | 182.55 | McCullough and Messerly, 1961 | DH |
78.81 | 182.56 | Douglas, Furukawa, et al., 1954 | DH |
76.81 | 182.56 | Ginnings and Furukawa, 1953 | DH |
76.93 | 182.52 | Pitzer K.S., 1940 | DH |
77.0 | 182.7 | Meijer, Blok, et al., 1977 | DH |
77.02 | 182.56 | Van Miltenburg, 1972 | DH |
76.81 | 182.56 | Oetting F.L., 1963 | DH |
77.73 | 182.2 | Huffman, Parks, et al., 1930 | DH |
77.73 | 182.2 | Parks, Huffman, et al., 1930 | DH |
Temperature of phase transition
Ttrs (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|
182.586 | crystaline, I | liquid | Holzhauer and Ziegler, 1975 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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 |
---|---|---|---|---|
0.0012 | 3700. | L | N/A | |
0.0012 | 3700. | X | N/A | |
0.00037 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.00044 | L | N/A | ||
0.00049 | V | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
L - Sharon G. Lias
Data compiled as indicated in comments:
LL - Sharon G. Lias and Joel F. Liebman
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.93 ± 0.10 | eV | N/A | N/A | L |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.15 | EST | Luo and Pacey, 1992 | LL |
9.93 ± 0.10 | EVAL | Lias, 1982 | LBLHLM |
9.83 ± 0.15 | EQ | Mautner(Meot-Ner), Sieck, et al., 1981 | LLK |
9.91 | EQ | Lias, Ausloos, et al., 1976 | LLK |
9.90 ± 0.05 | PI | Brehm, 1966 | RDSH |
10.16 | PE | Turner and Al-Joboury, 1964 | RDSH |
10.08 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH3+ | 27.9 ± 0.2 | ? | EI | Olmsted, Street, et al., 1964 | RDSH |
C2H5+ | 12.89 | ? | EI | Potzinger and Bunau, 1969 | RDSH |
C3H5+ | 12.7 ± 0.1 | ? | PI | Brehm, 1966 | RDSH |
C3H6+ | 10.7 ± 0.1 | C4H10 | PI | Brehm, 1966 | RDSH |
C3H6+ | 10.97 ± 0.08 | C4H10 | PI | Steiner, Giese, et al., 1961 | RDSH |
C3H7+ | 11.58 | ? | EI | Potzinger and Bunau, 1969 | RDSH |
C3H7+ | 11.05 ± 0.05 | ? | PI | Brehm, 1966 | RDSH |
C4H7+ | 11.5 ± 0.1 | ? | PI | Brehm, 1966 | RDSH |
C4H8+ | 10.56 ± 0.05 | C3H8 | PI | Brehm, 1966 | RDSH |
C4H8+ | 10.97 ± 0.03 | C3H8 | PI | Steiner, Giese, et al., 1961 | RDSH |
C4H9+ | 10.72 | C3H7 | EI | Potzinger and Bunau, 1969 | RDSH |
C4H9+ | 10.56 ± 0.05 | C3H7 | PI | Brehm, 1966 | RDSH |
C4H9+ | 11.19 ± 0.07 | C3H7 | PI | Steiner, Giese, et al., 1961 | RDSH |
C5H10+ | 10.33 | C2H6 | EI | Lewis and Hamill, 1970 | RDSH |
C5H10+ | 10.40 ± 0.05 | C2H6 | PI | Brehm, 1966 | RDSH |
C5H10+ | 11.035 ± 0.025 | C2H6 | PI | Steiner, Giese, et al., 1961 | RDSH |
C5H11+ | 10.66 | C2H5 | EI | Potzinger and Bunau, 1969 | RDSH |
C5H11+ | 10.43 ± 0.05 | C2H5 | PI | Brehm, 1966 | RDSH |
C5H11+ | 10.96 ± 0.085 | C2H5 | PI | Steiner, Giese, et al., 1961 | RDSH |
C6H12+ | 11.145 ± 0.035 | CH4 | PI | Steiner, Giese, et al., 1961 | RDSH |
C6H13+ | 10.7 ± 0.1 | CH3 | PI | Brehm, 1966 | RDSH |
C6H13+ | 10.93 ± 0.11 | CH3 | PI | Steiner, Giese, et al., 1961 | RDSH |
IR Spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Mass spectrum (electron ionization), References, Notes
Data compiled by: Coblentz Society, Inc.
- GAS (30 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg); DOW KBr FOREPRISM-GRATING; DIGITIZED BY COBLENTZ SOCIETY (BATCH II) FROM HARD COPY; 2 cm-1 resolution
- LIQUID (NEAT); DOW KBr FOREPRISM-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
Mass spectrum (electron ionization)
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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 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 | D.HENNEBERG, MAX-PLANCK INSTITUTE, MULHEIM, WEST GERMANY |
NIST MS number | 61276 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D.,
Heats of combustion and formation of the paraffin hydrocarbons at 25° C,
J. Res. NBS, 1945, 263-267. [all data]
Davies and Gilbert, 1941
Davies, G.F.; Gilbert, E.C.,
Heats of combustion and formation of the nine isomeric heptanes in the liquid state,
J. Am. Chem. Soc., 1941, 63, 2730-2732. [all data]
Scott D.W., 1974
Scott D.W.,
Chemical Thermodynamic Properties of Hydrocarbons and Related Substances. Properties of the Alkane Hydrocarbons, C1 through C10 in the Ideal Gas State from 0 to 1500 K. U.S. Bureau of Mines, Bulletin 666, 1974. [all data]
Scott D.W., 1974, 2
Scott D.W.,
Correlation of the chemical thermodynamic properties of alkane hydrocarbons,
J. Chem. Phys., 1974, 60, 3144-3165. [all data]
Pitzer K.S., 1944
Pitzer K.S.,
Thermodynamics of gaseous paraffins. Specific heat and related properties,
Ind. Eng. Chem., 1944, 36, 829-831. [all data]
Pitzer K.S., 1946
Pitzer K.S.,
The entropies and related properties of branched paraffin hydrocarbons,
Chem. Rev., 1946, 39, 435-447. [all data]
Waddington G., 1947
Waddington G.,
An improved flow calorimeter. Experimental vapor heat capacities and heats of vaporization of n-heptane and 2,2,3-trimethylbutane,
J. Am. Chem. Soc., 1947, 69, 22-30. [all data]
Huffman, Gross, et al., 1961
Huffman, H.M.; Gross, M.E.; Scott, D.W.; McCullough, I.P.,
Low temperature thermodynamic properties of six isomeric heptanes,
J. Phys. Chem., 1961, 65, 495-503. [all data]
Douglas, Furukawa, et al., 1954
Douglas, T.B.; Furukawa, G.T.; McCoskey, R.E.; Ball, A.F.,
Calorimetric properties of normal heptane from 0 to 520 K,
J. Res., 1954, NBS 53, 139-153. [all data]
Pitzer K.S., 1940
Pitzer K.S.,
The thermodynamics of n-heptane and 2,2,4-trimethylpentane, including heat capacities, heats of fusion and vaporization and entropies,
J. Am. Chem. Soc., 1940, 62, 1224-1227. [all data]
Huffman, Parks, et al., 1930
Huffman, H.M.; Parks, G.S.; Thomas, S.B.,
Thermal data on organic compounds. VIII. The heat capacities, entropies and free energies of the isomeric heptanes,
J. Am. Chem. Soc., 1930, 52, 3241-3251. [all data]
Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B.,
Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]
Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M.,
Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc.,
Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]
Saito and Tanaka, 1988
Saito, A.; Tanaka, R.,
Excess volumes and heat capacities of binary mixtures formed from cyclohexane, hexane and heptane at 298.15 K,
J. Chem. Thermodynam., 1988, 20, 859-865. [all data]
Shiohama, Ogawa, et al., 1988
Shiohama, Y.; Ogawa, H.; Murakami, S.; Fujihara, I.,
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Kalali, H.; Kohler, F.; Svejda, P.,
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Excess heat capacities for mixture of benzene with n-heptane at 293.15, 298.15 and 303.15 K,
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Van Miltenburg, J.C.; Van den Berg, G.J.K.; Van Bommel, M.J.,
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Excess enthalpy, excess heat capacity and excess volume of 1,2,4-trimethylbenzene +, and 1-methylnaphthalene + an n-alkane,
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Tanaka, R.,
Determination of excess heat capacities of (benzene + tetrachloromethane and + cyclohexane) between 293.15 and 303.15 K by use of a Picker flow calorimeter,
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Experimental study of the isobaric heat capacity of liquid organic compounds with molecular weights of up to 4000 a.e.m., 1982, Teplomassoobmen Teplofiz. [all data]
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Brown, G.N., Jr.; Ziegler, W.T.,
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Excess heat capacities of binary liquid mixtures determined with a Picker flow calorimeter,
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Van Miltenburg, J.C.,
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Oetting F.L.,
The heat capacity and entropy of 2-methyl-2-propanol from 15 to 330 K,
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Helfrey, P.F.; Heiser, D.A.; Sage, B.H.,
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Heat capacity standards for the range 14 to 1200°K,
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Heat of mixing of liquids,
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Phillip, N.M.,
Adiabatic and isothermal compressibilities of liquids,
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Vold, R.D.,
A calorimetric test of the solubility equation for regular solutions,
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Richards, W.T.; Wallace, J.H., Jr.,
The specific heats of five organic liquids from their adiabatic temperature-pressure coefficients,
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Forziati, Alphonse F.; Norris, William R.; Rossini, Frederick D.,
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Vapour pressures and excess Gibbs free energies of (cyclohexanol + n-heptane) between 303.147 and 373.278 K,
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Waddington, Guy; Todd, Samuel S.; Huffman, Hugh M.,
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Thomson, George Wm.,
The Antoine Equation for Vapor-pressure Data.,
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Vapor pressures and boiling points of some paraffin, alkylcyclopentane, alkylcyclohexane, and alkylbenzene hydrocarbons,
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Smith, E.R.,
Boiling points of n-heptane and 2,2,4-trimethylpentane over the range 100- to 1,500-millimeter pressure,
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Carruth, Grant F.; Kobayashi, Riki,
Vapor pressure of normal paraffins ethane through n-decane from their triple points to about 10 mm mercury,
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Williamham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D.,
Vapor Pressures and Boiling Points of Some Paraffin, Alkylcyclopentane, Alkylcyclohexane, and Alkylbenzene Hydrocarbons,
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Thermochemical information from ion-molecule rate constants,
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Brehm, B.,
Massenspektrometrische Untersuchung der Photoionisation von Molekulen,
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Molecular photoelectron spectroscopy,
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Ionization potentials of some molecules,
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Excess-kinetic-energy ions in organic mass spectra,
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Empirische Beruksichtigung von Uberschussenergien bei der Auftrittspotentialbestimmung,
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Photoionization of alkanes. Dissociation of excited molecular ions,
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Excited states of neutral molecular fragments from appearance potentials by electron impact in a mass spectrometer,
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Ttrs Temperature of phase transition 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 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 ΔsubH Enthalpy of sublimation 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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