Cyclopropane
- Formula: C3H6
- Molecular weight: 42.0797
- IUPAC Standard InChIKey: LVZWSLJZHVFIQJ-UHFFFAOYSA-N
- CAS Registry Number: 75-19-4
- 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: Trimethylene; Trimethylene (cyclic); UN 1027; Cyclopropnane
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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:
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 | 39.30 | kJ/mol | Cm | Lacher, Walden, et al., 1950 | Heat of hydrobromination; ALS |
ΔfH°gas | 53.30 ± 0.59 | kJ/mol | Cm | Knowlton and Rossini, 1949 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -2091.4 ± 0.54 | kJ/mol | Cm | Knowlton and Rossini, 1949 | Corresponding ΔfHºgas = 53.35 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.26 | 50. | Dorofeeva O.V., 1986 | Selected S(T) and Cp(T) values are in good agreement with those calculated earlier [ Kobe K.A., 1950]. The agreement with the data of [80KAR/PAM] increases as the temperature increases (up to 2 J/mol*K in Cp(1000 K)).; GT |
33.32 | 100. | ||
34.56 | 150. | ||
38.91 | 200. | ||
50.69 | 273.15 | ||
55.6 ± 1.0 | 298.15 | ||
55.94 | 300. | ||
76.05 | 400. | ||
93.86 | 500. | ||
108.54 | 600. | ||
120.68 | 700. | ||
130.91 | 800. | ||
139.66 | 900. | ||
147.21 | 1000. | ||
153.75 | 1100. | ||
159.43 | 1200. | ||
164.38 | 1300. | ||
168.69 | 1400. | ||
172.45 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.38 | 157.8 | Kistiakowsky G.B., 1940 | Please also see Kistiakowsky G.B., 1940, 2.; GT |
42.16 | 220.1 | ||
42.55 | 223.7 | ||
48.68 | 258.7 | ||
50.63 | 272.15 | ||
54.66 | 291.4 | ||
55.25 | 295.5 | ||
56.48 | 300.48 | ||
59.29 | 313.9 | ||
59.27 | 316.7 | ||
60.90 | 325.1 | ||
62.17 | 332.8 | ||
63.18 | 333.70 | ||
64.27 | 338.9 | ||
63.26 | 339.6 | ||
70.17 | 368.46 |
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 by: Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 142.63 | J/mol*K | N/A | Ruehrwein and Powell, 1946 |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
81.34 | 240. | Ruehrwein and Powell, 1946 | T = 14 to 240 K. |
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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 240. ± 3. | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 146. ± 3. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 145.8 | K | N/A | Tickner and Lossing, 1951 | Uncertainty assigned by TRC = 0.8 K; from change in slope of obs. vapor pressure; TRC |
Ttriple | 145.57 | K | N/A | Ruehrwein and Powell, 1946, 2 | Uncertainty assigned by TRC = 0.02 K; temp. scale for Tc = 273.10K; TRC |
Ttriple | 145.59 | K | N/A | Ruehrwein and Powell, 1946, 2 | Uncertainty assigned by TRC = 0.08 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 398.0 ± 0.3 | K | N/A | Daubert, 1996 | |
Tc | 398.3 | K | N/A | Lin, Silberberg, et al., 1970 | Uncertainty assigned by TRC = 0.05 K; TRC |
Tc | 397.80 | K | N/A | Booth and Morris, 1958 | Uncertainty assigned by TRC = 0.15 K; mean of measurements on three samples by visual obssrvation; TRC |
Tc | 397.8 | K | N/A | Horneg, 1941 | Uncertainty assigned by TRC = 1. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 55.4 ± 0.5 | bar | N/A | Daubert, 1996 | |
Pc | 55.7946 | bar | N/A | Lin, Silberberg, et al., 1970 | Uncertainty assigned by TRC = 0.0506 bar; TRC |
Pc | 54.95 | bar | N/A | Booth and Morris, 1958 | Uncertainty assigned by TRC = 0.2026 bar; mean of measurements on 3 samples, visual observation; TRC |
Pc | 3.274 | bar | N/A | Horneg, 1941 | Uncertainty assigned by TRC = 0.01 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.162 | l/mol | N/A | Daubert, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 6.15 ± 0.05 | mol/l | N/A | Daubert, 1996 | |
ρc | 6.143 | mol/l | N/A | Lin, Silberberg, et al., 1970 | Uncertainty assigned by TRC = 0.007 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 18.11 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 17.02 | kJ/mol | N/A | Lin, Silberberg, et al., 1970, 2 | AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
20.054 | 240.34 | N/A | Ruehrwein and Powell, 1946 | P = 101.325 kPa; DH |
20.05 | 240.3 | N/A | Majer and Svoboda, 1985 | |
21.8 | 210. | N/A | Calado, Filipe, et al., 1997 | Based on data from 195. to 225. K.; AC |
20.4 | 373. | A | Stephenson and Malanowski, 1987 | Based on data from 358. to 398. K.; AC |
19.9 | 312. | A | Stephenson and Malanowski, 1987 | Based on data from 297. to 359. K.; AC |
20.3 | 224. | A | Stephenson and Malanowski, 1987 | Based on data from 188. to 239. K.; AC |
19.9 | 254. | A | Stephenson and Malanowski, 1987 | Based on data from 239. to 298. K.; AC |
21.1 | 226. | N/A | Ruehrwein and Powell, 1946, 3 | Based on data from 183. to 241. K. See also Boublik, Fried, et al., 1984.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
83.44 | 240.34 | Ruehrwein and Powell, 1946 | 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 |
---|---|---|---|---|---|
183.12 to 241.07 | 4.05015 | 870.393 | -25.063 | Ruehrwein and Powell, 1946, 3 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
29.2 | 145. | B | Bondi, 1963 | AC |
28.2 | 128. | A,MS | Tickner and Lossing, 1951, 2 | Based on data from 115. to 141. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
5.443 | 145.57 | Ruehrwein and Powell, 1946 | DH |
5.44 | 145.6 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
37.39 | 145.57 | Ruehrwein and Powell, 1946 | 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:
B - John E. Bartmess
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
C3H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1716. ± 10. | kJ/mol | AVG | N/A | Average of 5 out of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1676. ± 10. | kJ/mol | AVG | N/A | Average of 3 out of 6 values; Individual data points |
By formula: HBr + C3H6 = C3H7Br
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -107.8 ± 1.3 | kJ/mol | Cm | Lacher, Kianpour, et al., 1957 | gas phase; ALS |
ΔrH° | -94.94 ± 0.65 | kJ/mol | Cm | Lacher, Walden, et al., 1950 | gas phase; Heat of hydrobromination; ALS |
By formula: C3H6I2 = C3H6 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 77. ± 17. | kJ/mol | Eqk | Benson and Amano, 1962 | gas phase; ALS |
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 |
---|---|---|---|---|
0.013 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. Value at T = 294. K. | |
0.011 | 1700. | L | N/A |
Gas phase ion energetics 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
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
View reactions leading to C3H6+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.86 ± 0.04 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 750.3 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 722.2 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.90 | PI | Traeger, 1984 | LBLHLM |
9.86 | EQ | Lias and Buckley, 1984 | LBLHLM |
10.60 | PE | Kimura, Katsumata, et al., 1981 | LLK |
9.8 ± 0.1 | PE | Bieri, Burger, et al., 1977 | LLK |
10.3 ± 0.1 | EI | Rothgery, Holt, et al., 1975 | LLK |
9.91 ± 0.03 | PI | Krassig, Reinke, et al., 1974 | LLK |
≤9.93 | EI | Lossing, 1972 | LLK |
≤9.8 | PE | Basch, Robin, et al., 1969 | RDSH |
10.1 | CI | Cermak, 1968 | RDSH |
10.06 ± 0.03 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
10.54 | PE | Plemenkov, Villem, et al., 1981 | Vertical value; LLK |
10.6 ± 0.1 | PE | Bieri, Burger, et al., 1977 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH2+ | 19.3 | C2H4 | EI | Haney and Franklin, 1968 | RDSH |
C2H2+ | 12.71 ± 0.06 | CH4 | PI | Krassig, Reinke, et al., 1974 | LLK |
C2H2+ | 13.1 | CH4 | EI | Haney and Franklin, 1968 | RDSH |
C2H3+ | 12.64 ± 0.05 | CH3 | PI | Krassig, Reinke, et al., 1974 | LLK |
C2H3+ | 13.4 | CH3 | EI | Haney and Franklin, 1968 | RDSH |
C2H3+ | 13.3 ± 0.2 | CH3 | EI | Harrison and Tait, 1962 | RDSH |
C3H+ | 19.7 ± 0.5 | 2H2+H | EI | Harrison and Tait, 1962 | RDSH |
C3H3+ | 12.1 ± 0.1 | H2+H(-) | PI | Krassig, Reinke, et al., 1974 | LLK |
C3H3+ | 12.9 ± 0.1 | H2+H | PI | Krassig, Reinke, et al., 1974 | LLK |
C3H3+ | 13.7 ± 0.1 | H2+H | EI | Harrison and Tait, 1962 | RDSH |
C3H4+ | 11.64 ± 0.15 | H2 | PI | Krassig, Reinke, et al., 1974 | LLK |
C3H4+ | 11.6 ± 0.1 | H2 | EI | Harrison and Tait, 1962 | RDSH |
C3H5+ | 11.43 | H | PI | Traeger, 1984 | LBLHLM |
C3H5+ | 11.47 | H | PI | Buttrill, Williamson, et al., 1975 | LLK |
C3H5+ | 10.74 ± 0.09 | H(-) | PI | Krassig, Reinke, et al., 1974 | LLK |
C3H5+ | 11.44 ± 0.05 | H | PI | Krassig, Reinke, et al., 1974 | LLK |
C3H5+ | 11.49 | H | EI | Lossing, 1972 | LLK |
De-protonation reactions
C3H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1716. ± 10. | kJ/mol | AVG | N/A | Average of 5 out of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1676. ± 10. | kJ/mol | AVG | N/A | Average of 3 out of 6 values; Individual data points |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
- GAS; Not specified, most likely a prism, grating, or hybrid spectrometer.; DIGITIZED BY NIST FROM HARD COPY; 4 cm-1 resolution
- GAS (100 mmHg DILUTED TO A TOTAL PRESSURE OF 400 mmHg WITH N2); DOW KBr FOREPRISM-GRATING; DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 cm-1 resolution
- GAS (100 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg); DOW KBr FOREPRISM-GRATING; DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 2 cm-1 resolution
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. |
---|---|
NIST MS number | 18855 |
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: D3h Symmetry Number σ = 6
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a1' | 1 | CH2 s-str | 3038 | C | ia | 3038 S p | gas | |||
a1' | 2 | CH2 scis | 1479 | D | ia | 1504 W p | gas | FR(2ν14) | ||
a1' | 2 | CH2 scis | 1479 | D | ia | 1453 W p | gas | FR(2ν14) | ||
a1' | 3 | Ring str | 1188 | C | ia | 1188 S p | gas | |||
a1 | 4 | CH2 twist | 1126 | D | 1126 ia VW | gas | 1133 ia | gas | ||
a2' | 5 | CH2 wag | 1070 | D | 1075 ia | sln. | ia | OC(ν5+ν10) | ||
a2 | 6 | CH2 a-str | 3103 | C | 3103 S | gas | ia | |||
a2 | 7 | CH2 rock | 854 | C | 854 S | gas | ia | |||
e' | 8 | CH2 s-str | 3025 | C | 3025 VS | gas | 3020 VS p | gas | ||
e' | 9 | CH2 scis | 1438 | C | 1438 M | gas | 1442 M dp | gas | ||
e' | 10 | CH2 wag | 1029 | C | 1029 S | gas | 1023 VW | liq. | ||
e' | 11 | Ring deform | 866 | C | 866 VS | gas | 866 S dp | gas | ||
e | 12 | CH2 a-str | 3082 | C | ia | 3082 S dp | gas | |||
e | 13 | CH2 twist | 1188 | C | ia | 1188 M dp | gas | |||
e | 14 | CH2 rock | 739 | C | ia | 739 W dp | gas | |||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
ia | Inactive |
p | Polarized |
dp | Depolarized |
FR | Fermi resonance with an overtone or a combination tone indicated in the parentheses. |
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 |
Gas Chromatography
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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
Kovats' RI, non-polar column, isothermal
Column type | Active phase | Temperature (C) | I | Reference | Comment |
---|---|---|---|---|---|
Capillary | BPX-5 | 30. | 356. | Aflalaye, Sternberg, et al., 1995 | 12. m/0.15 mm/0.25 μm, H2 |
Capillary | BPX-5 | 30. | 357. | Aflalaye, Sternberg, et al., 1995 | 12. m/0.15 mm/0.25 μm, H2 |
Capillary | CP Sil 5 CB | 20. | 348.8 | Do and Raulin, 1992 | 25. m/0.15 mm/2. μm, H2 |
Packed | Squalane | 27. | 344. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 49. | 345. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 67. | 346. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 86. | 347. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Van Den Dool and Kratz RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Packed | SE-30 | 367. | Peng, Ding, et al., 1988 | Supelcoport; Chromosorb; Column length: 3.05 m; Program: 40C(5min) => 10C/min => 200C or 250C (60min) |
Normal alkane RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | OV-101 | 331. | Zenkevich, 2005 | 25. m/0.20 mm/0.10 μm, N2/He, 6. K/min; Tstart: 50. C; Tend: 250. C |
Normal alkane RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Polydimethyl siloxanes | 331. | Zenkevich, Chupalov, et al., 1996 | Program: not specified |
Packed | SE-30 | 351. | Robinson and Odell, 1971 | N2, Chromosorb W; Column length: 6.1 m; Program: 50C910min) => 20C/min => 90(6min) => 10C/min => 150C(hold) |
Normal alkane RI, polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-Wax | 405. | Peng, Yang, et al., 1991 | Program: not specified |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), Vibrational and/or electronic energy levels, Gas Chromatography, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Lacher, Walden, et al., 1950
Lacher, J.R.; Walden, C.H.; Lea, K.R.; Park, J.D.,
Vapor phase heats of hydrobromination of cyclopropane and propylene,
J. Am. Chem. Soc., 1950, 72, 331-333. [all data]
Knowlton and Rossini, 1949
Knowlton, J.W.; Rossini, F.D.,
Heats of combustion and formation of cyclopropane,
J. Res. NBS, 1949, 43, 113-115. [all data]
Dorofeeva O.V., 1986
Dorofeeva O.V.,
Thermodynamic properties of twenty-one monocyclic hydrocarbons,
J. Phys. Chem. Ref. Data, 1986, 15, 437-464. [all data]
Kobe K.A., 1950
Kobe K.A.,
Thermochemistry for the petrochemical industry. XIV. Some miscellaneous hydrocarbons,
Petrol. Refiner, 1950, 29 (12), 93-96. [all data]
Kistiakowsky G.B., 1940
Kistiakowsky G.B.,
Gaseous heat capacities. II,
J. Chem. Phys., 1940, 8, 610-618. [all data]
Kistiakowsky G.B., 1940, 2
Kistiakowsky G.B.,
The low temperature gaseous heat capacities of certain C3 hydrocarbons,
J. Chem. Phys., 1940, 8, 970-977. [all data]
Ruehrwein and Powell, 1946
Ruehrwein, R.A.; Powell, T.M.,
The heat capacity, vapor pressure, heats of fusion and vaporization of cyclopropane. Entropy and density of the gas,
J. Am. Chem. Soc., 1946, 68, 1063-1068. [all data]
Tickner and Lossing, 1951
Tickner, A.W.; Lossing, F.P.,
The Measurement of Low Vapor Pressures by Means of A Mass Spectrometer,
J. Phys. Colloid Chem., 1951, 55, 733-40. [all data]
Ruehrwein and Powell, 1946, 2
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The heat capacity, vapor pressure, heats of fusion and vaporization of cyclopropane. Entropy and density of the gas,
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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 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°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas 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 ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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