Ethane, 1,2-dichloro-
- Formula: C2H4Cl2
- Molecular weight: 98.959
- IUPAC Standard InChIKey: WSLDOOZREJYCGB-UHFFFAOYSA-N
- CAS Registry Number: 107-06-2
- 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: α,β-Dichloroethane; s-Dichloroethane; Brocide; Dutch liquid; Ethylene chloride; Ethylene dichloride; Freon 150; Glycol dichloride; 1,2-Bichloroethane; 1,2-Dichlorethane; 1,2-Dichloroethane; CH2ClCH2Cl; sym-Dichloroethane; Aethylenchlorid; Bichlorure D'ethylene; Borer sol; Chlorure D'ethylene; Cloruro di ethene; 1,2-DCE; Destruxol borer-sol; 1,2-Dichloorethaan; 1,2-Dichlor-aethan; Dichloremulsion; Di-chlor-mulsion; Dichloro-1,2-ethane; 1,2-Dicloroetano; Dutch oil; EDC; ENT 1,656; Ethane dichloride; Ethyleendichloride; 1,2-Ethylene dichloride; NCI-C00511; Rcra waste number U077; UN 1184; DCE; EDC (halocarbon); HCC 150; 1,2-dichloroethane (ethylene dichloride)
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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
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -31.5 ± 0.84 | kcal/mol | Review | Manion, 2002 | derived from recommended ΔfHliquid° and ΔvapH°; DRB |
ΔfH°gas | -29.98 ± 0.25 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | Reanalyzed by Cox and Pilcher, 1970, Original value = -30.18 ± 0.25 kcal/mol; At 250 C; ALS |
ΔfH°gas | -30.8 | kcal/mol | Cm | Kirkbride, 1956 | Heat of chlorination; ALS |
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:
DRB - Donald R. Burgess, Jr.
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 | -39.96 ± 0.84 | kcal/mol | Review | Manion, 2002 | weighted average of several measurements; DRB |
ΔfH°liquid | -40.55 | kcal/mol | Ccr | Hu and Sinke, 1969 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -295.51 | kcal/mol | Ccr | Hu and Sinke, 1969 | ALS |
ΔcH°liquid | -297.9 ± 2.0 | kcal/mol | Ccb | Smith, Bjellerup, et al., 1953 | Reanalyzed by Cox and Pilcher, 1970, Original value = -297. ± 2. kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 49.840 | cal/mol*K | N/A | Pitzer, 1940 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
30.93 | 298.15 | Hallen, 1993 | DH |
30.786 | 298.15 | Lainez, Roux-Desgranges, et al., 1985 | DH |
30.829 | 298.15 | Wilhelm, Faradjzadeh, et al., 1979 | DH |
30.83 | 298.15 | Wilhelm, Grolier, et al., 1979 | DH |
30.829 | 298.15 | Wilhelm, Grolier, et al., 1977 | DH |
30.74 | 298.15 | Wilhelm, Schano, et al., 1969 | T = 20, 30 40°C.; DH |
30.88 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 353 K.; DH |
30.961 | 298.15 | Ruiter, 1955 | T = 7 to 50°C.; DH |
30.999 | 298. | Staveley, Tupman, et al., 1955 | T = 284 to 348 K.; DH |
29.71 | 293. | Sieg, Crtzen, et al., 1951 | DH |
29.40 | 298. | Kurbatov, 1948 | T = -25 to 86°C, mean Cp, four temperatures.; DH |
30.81 | 298.15 | Pitzer, 1940 | T = 15 to 308 K.; DH |
31.31 | 300. | Railing, 1939 | T = 90 to 320 K. Data graphically only. Value read from graph.; DH |
29.21 | 298. | von Reis, 1881 | T = 290 to 364 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:
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
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
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 | 356.7 ± 0.6 | K | AVG | N/A | Average of 48 out of 52 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 230. ± 40. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 237.6 | K | N/A | Knauth and Sabbah, 1990 | Uncertainty assigned by TRC = 0.3 K; TRC |
Ttriple | 237.2 | K | N/A | Pitzer, 1940, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 561.6 | K | N/A | Garcia-Sanchez and Trejo Rodriguez, 1985 | Uncertainty assigned by TRC = 0.4 K; TRC |
Tc | 561.2 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 563.15 | K | N/A | Hojendahl, 1946 | Uncertainty assigned by TRC = 3. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 53.10 | atm | N/A | Garcia-Sanchez and Trejo Rodriguez, 1985 | Uncertainty assigned by TRC = 0.49 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.45 | mol/l | N/A | Hojendahl, 1946 | Uncertainty assigned by TRC = 0.15 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 8.4 ± 0.1 | kcal/mol | AVG | N/A | Average of 8 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
7.643 | 356.6 | N/A | Majer and Svoboda, 1985 | |
7.43 | 371. | A | Stephenson and Malanowski, 1987 | Based on data from 356. to 558. K.; AC |
8.32 | 294. | A | Stephenson and Malanowski, 1987 | Based on data from 279. to 374. K.; AC |
7.43 | 383. | A | Stephenson and Malanowski, 1987 | Based on data from 368. to 524. K.; AC |
9.75 | 538. | A | Stephenson and Malanowski, 1987 | Based on data from 523. to 561. K.; AC |
8.32 | 294. | N/A | Stephenson and Malanowski, 1987 | Based on data from 279. to 434. K. See also Dykyj, 1970.; AC |
8.29 | 316. | N/A | Gutsche and Knapp, 1982 | Based on data from 301. to 357. K.; AC |
8.105 | 273. | V | Gallaugher and Hibbert, 1937 | ALS |
8.96 | 258. | N/A | Pearce and Peters, 1928 | Based on data from 243. to 372. K.; AC |
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 |
---|---|---|---|---|---|
242.33 to 372.6 | 4.57947 | 1521.789 | -24.67 | Pearce and Peters, 1929 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.1120 | 237.2 | Pitzer, 1940 | DH |
2.11 | 237.2 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.903 | 237.2 | Pitzer, 1940 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.87 | 237.2 | Domalski and Hearing, 1996 | CAL |
8.80 | 175. |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.6800 | 175. | crystaline, II | Railing, 1939 | DH | |
2.090 | 237.6 | crystaline, I | liquid | Railing, 1939 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
3.87 | 175. | crystaline, II, Lambda | , type transition | Railing, 1939 | DH |
8.80 | 237.6 | crystaline, I | liquid | Railing, 1939 | 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 by: 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: C2H4Cl2 = C2H3Cl + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12.1 ± 1.0 | kcal/mol | Cm | Buravtsev, Grigor'ev, et al., 1992 | gas phase |
ΔrH° | 19.6 | kcal/mol | Eqk | Levanova, Bushneva, et al., 1979 | liquid phase |
ΔrH° | 16.3 | kcal/mol | Eqk | Levanova, Bushneva, et al., 1979 | gas phase |
ΔrH° | 16.24 | kcal/mol | Eqk | Ghosh and Guha, 1951 | liquid phase |
By formula: C2H4Cl2 + 2H2 = C2H6 + 2HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -34.18 ± 0.23 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -35.32 ± 0.12 kcal/mol; At 250 C |
By formula: C2H4Cl2 + Cl2 = HCl + C2H3Cl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -27.8 | kcal/mol | Cm | Kirkbride, 1956 | liquid phase; Heat of chlorination |
By formula: C2H4Cl2 = C2H4Cl2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.30 ± 0.33 | kcal/mol | Eqk | Rozhnov, 1968 | gas phase; Heat of isomerization at 385 K |
By formula: C2H4 + Cl2 = C2H4Cl2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -43.65 ± 0.15 | kcal/mol | Cm | Conn, Kistiakowsky, et al., 1938 | gas phase; At 355 °K |
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 |
---|---|---|---|---|
0.72 | 4200. | L | N/A | |
0.95 | 4300. | M | N/A | |
0.83 | M | N/A | ||
0.82 | 3800. | X | N/A | |
0.87 | 3900. | M | N/A | |
0.85 | 3900. | X | N/A | |
0.84 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.64 | 4500. | X | N/A | |
0.69 | 4700. | X | N/A | |
0.64 | 1500. | X | N/A | |
0.86 | 3700. | X | Barr and Newsham, 1987 | |
0.90 | 2400. | X | N/A | |
0.84 | 3500. | X | Leighton and Calo, 1981 | |
0.92 | L | N/A | ||
0.81 | V | N/A | ||
1.0 | C | N/A | ||
0.76 | V | N/A | ||
1.1 | M | Pearson and McConnell, 1975 | The same data was also published in missing citation. Value at T = 293. K. | |
0.83 | 4100. | M | 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:
L - Sharon G. Lias
Data compiled as indicated in comments:
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) | 11.07 ± 0.04 | eV | N/A | N/A | L |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
11.05 | PI | Berman, Anicich, et al., 1979 | LLK |
11.04 | PE | Berman, Anicich, et al., 1979 | LLK |
11.12 ± 0.05 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
11.40 ± 0.10 | PE | Gan, Peel, et al., 1977 | Vertical value; Trans conformer; LLK |
11.22 ± 0.02 | PE | Chau and McDowell, 1975 | Vertical value; LLK |
11.39 ± 0.03 | PE | Raymonda, Edwards, et al., 1974 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH2Cl+ | 12.5 ± 0.1 | CH2Cl | EI | Harrison and Shannon, 1962 | RDSH |
C2H3Cl+ | 11.1 | ? | PI | Berman, Anicich, et al., 1979 | LLK |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
- Not specified, most likely a prism, grating, or hybrid spectrometer.; DIGITIZED BY NIST FROM HARD COPY; 4 cm-1 resolution
- GAS (50 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg); DOW KBr FOREPRISM-GRATING; DIGITIZED BY COBLENTZ SOCIETY (BATCH II) FROM HARD COPY; 2 cm-1 resolution
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Data compiled by: Pamela M. Chu, Franklin R. Guenther, George C. Rhoderick, and Walter J. Lafferty
- gas; IFS66V (Bruker); 3-Term B-H Apodization
0.1250, 0.2410, 0.4820, 0.9640, 1.9290 cm-1 resolution - gas; IFS66V (Bruker); Boxcar Apodization
0.1250, 0.2410, 0.4820, 0.9640, 1.9290 cm-1 resolution - gas; IFS66V (Bruker); Happ Genzel Apodization
0.1250, 0.2410, 0.4820, 0.9640, 1.9290 cm-1 resolution - gas; IFS66V (Bruker); NB Strong Apodization
0.1250, 0.2410, 0.4820, 0.9640, 1.9290 cm-1 resolution - gas; IFS66V (Bruker); Triangular Apodization
0.1250, 0.2410, 0.4820, 0.9640, 1.9290 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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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 | NIST Mass Spectrometry Data Center, 1990. |
NIST MS number | 114952 |
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
Trans form Symmetry: C2h Symmetry Number σ = 2
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
ag | 1 | CH2 s-str | 2957 | D | ia | 2957 p | liq. | |||
ag | 2 | CH2 scis | 1445 | C | ia | 1445 dp | liq. | |||
ag | 3 | CH2 wag | 1304 | C | ia | 1304 p | liq. | |||
ag | 4 | CC str | 1052 | C | ia | 1052 p | liq. | |||
ag | 5 | CCl str | 754 | C | ia | 754 p | liq. | |||
ag | 6 | CCCl deform | 300 | C | ia | 300 p | liq. | |||
au | 7 | CH2 a-str | 3005 | D | 3005 W | liq. | ia | SF()gauche ν1, gauche ν11 | ||
au | 8 | CH2 twist | 1123 | B | 1122.5 W | gas | ia | |||
au | 9 | CH2 rock | 773 | B | 772.5 M | gas | ia | |||
au | 10 | Torsion | 123 | C | 123 M | gas | ia | |||
bg | 11 | CH2 a-str | 3005 | D | ia | 3005 dp | liq. | |||
bg | 12 | CH2 twist | 1264 | C | ia | 1264 dp | liq. | |||
bg | 13 | CH2 rock | 989 | C | ia | 989 p | liq. | |||
bu | 14 | CH2 s-str | 2983 | C | 2983.3 M | gas | ia | |||
bu | 15 | CH2 scis | 1461 | A | 1460.6 S | gas | ia | |||
bu | 16 | CH2 wag | 1232 | B | 1232.3 S | gas | ia | |||
bu | 17 | CCl str | 728 | C | 728.3 VS | gas | ia | |||
bu | 18 | CCCl deform | 222 | C | 222.3 W | gas | ia | |||
Source: Shimanouchi, 1972
Gauche form Symmetry: C2 Symmetry Number σ = 2
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a | 1 | CH2 a-str | 3005 | D | 3005 W | liq. | 3005 dp | liq. | SF(ν11, )trans ν7 | |
a | 2 | CH2 s-str | 2957 | D | 2957 M | liq. | 2957 p | liq. | SF()trans ν1, trans ν14 | |
a | 3 | CH2 scis | 1433 | C | 1433 M | liq. | 1429 dp | liq. | OV(ν13) | |
a | 4 | CH2 wag | 1315 | C | 1315 W | gas | 1304 | liq. | ||
a | 5 | CH2 twist | 1207 | C | 1207 p | liq. | ||||
a | 6 | CC str | 1027 | D | 1027 W | gas | 1031 dp | liq. | ||
a | 7 | CH2 rock | 948 | B | 947.7 M | gas | 943 p | liq. | ||
a | 8 | CCl str | 669 | C | 669 M | gas | 654 p | liq. | ||
a | 9 | CCCl deform | 272 | D | 272 VW | liq. | 265 p | liq. | ||
a | 10 | Torsion | 125 | liq. | ||||||
b | 11 | CH2 a-str | 3005 | D | 3005 W | gas | 3005 dp | liq. | SF(ν1, )trans ν7 | |
b | 12 | CH2 s-str | 2957 | C | 2957.2 W | gas | ||||
b | 13 | CH2 scis | 1436 | B | 1436.3 W | gas | ||||
b | 14 | CH2 wag | 1292 | B | 1292.1 S | gas | ||||
b | 15 | CH2 twist | 1146 | D | 1146 W | gas | 1145 dp | liq. | ||
b | 16 | CH2 rock | 890 | B | 890.3 M | gas | 881 dp | liq. | ||
b | 17 | CCl str | 693 | B | 692.5 W | gas | 677 dp | liq. | ||
b | 18 | CCCl deform | 410 | C | 409.6 M | gas | 411 dp | liq. | ||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
ia | Inactive |
p | Polarized |
dp | Depolarized |
SF | Calculation shows that the frequency approximately equals that of the vibration indicated in the parentheses. |
OV | Overlapped by band indicated in parentheses. |
A | 0~1 cm-1 uncertainty |
B | 1~3 cm-1 uncertainty |
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, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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.
Manion, 2002
Manion, J.A.,
Evaluated Enthalpies of Formation of the Stable Closed Shell C1 and C2 Chlorinated Hydrocarbons,
J. Phys. Chem. Ref. Data, 2002, 31, 1, 123-172, https://doi.org/10.1063/1.1420703
. [all data]
Lacher, Amador, et al., 1967
Lacher, J.R.; Amador, A.; Park, J.D.,
Reaction heats of organic compounds. Part 5.-Heats of hydrogenation of dichloromethane, 1,1- and 1,2-dichloroethane and 1,2-dichloropropane,
Trans. Faraday Soc., 1967, 63, 1608-1611. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Kirkbride, 1956
Kirkbride, F.W.,
The heats of chlorination of some hydrocarbons and their chloro-derivatives,
J. Appl. Chem., 1956, 6, 11-21. [all data]
Hu and Sinke, 1969
Hu, A.T.; Sinke, G.C.,
Combustion calorimetry of some chlorinated organic compounds,
J. Chem. Thermodyn., 1969, 1, 507-513. [all data]
Smith, Bjellerup, et al., 1953
Smith, L.; Bjellerup, L.; Krook, S.; Westermark, H.,
Heats of combustion of organic chloro compounds determined by the "quartz wool" method,
Acta Chem. Scand., 1953, 7, 65. [all data]
Pitzer, 1940
Pitzer, K.S.,
The heat capacities, heats of transition and fusion, and entropies of ethylene dichloride and ethylene dibromide,
J. Am. Chem. Soc., 1940, 62, 331-335. [all data]
Hallen, 1993
Hallen, D.,
Enthalpies of solution and heat capacities for some a,w-dichloroalkanes in water,
J. Chem. Thermodynam., 1993, 25, 519-524. [all data]
Lainez, Roux-Desgranges, et al., 1985
Lainez, A.; Roux-Desgranges, G.; Grolier, J.-P.E.; Wilhelm, E.,
Mixtures of alkanes with polar molecules showing integral rotation: an unusual composition dependence of CpE of 1,2-dichloroethane + an n-alkane,
Fluid Phase Equilib., 1985, 20, 47-56. [all data]
Wilhelm, Faradjzadeh, et al., 1979
Wilhelm, E.; Faradjzadeh, A.; Grolier, J.-P.E.,
Molar excess heat capacities and excess volumes of 1,2-dichloroethane + cyclooctane, + mesitylene, and + tetrachloromethane,
J. Chem. Thermodynam., 1979, 11, 979-984. [all data]
Wilhelm, Grolier, et al., 1979
Wilhelm, E.; Grolier, G.-P.E.; Karbalai Ghassemi, M.H.,
Molar heat capacity of binary liquid mixtures: 1,2-dichloroethane + cyclohexane and 1,2-dichloroethane + methylcyclohexane,
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The specific heat of some ethylene halides,
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Catalytic dehydrochlorination of ethylene dichloride,
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Notes
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- Symbols used in this document:
AE Appearance energy 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 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 ΔrH° Enthalpy 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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