Methane, iodo-
- Formula: CH3I
- Molecular weight: 141.9390
- IUPAC Standard InChIKey: INQOMBQAUSQDDS-UHFFFAOYSA-N
- CAS Registry Number: 74-88-4
- 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. - Isotopologues:
- Other names: Iodomethane; Methyl iodide; CH3I; Halon 10001; Iodometano; Iodure de methyle; Jod-methan; Joodmethaan; Methyljodid; Methyljodide; Metylu jodek; Monoioduro di metile; Rcra waste number U138; UN 2644; Methyl iodine; Monoiodomethane; NSC 9366
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Gas phase thermochemistry data
Go To: Top, 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), 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: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | 3.42 ± 0.34 | kcal/mol | Eqk | Golden, Walsh, et al., 1965 | Reanalyzed by Cox and Pilcher, 1970, Original value = 3.28 ± 0.16 kcal/mol |
ΔfH°gas | 3.50 ± 0.24 | kcal/mol | Eqk | Goy and Pritchard, 1965 | Reanalyzed by Cox and Pilcher, 1970, Original value = 3.40 ± 0.24 kcal/mol |
ΔfH°gas | 3.8 ± 0.3 | kcal/mol | Chyd | Carson, Carter, et al., 1961 |
Condensed phase thermochemistry data
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -3.3 ± 0.1 | kcal/mol | Ccr | Carson, Laye, et al., 1993 | ALS |
ΔfH°liquid | -2.9 ± 0.3 | kcal/mol | Chyd | Carson, Carter, et al., 1961 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -193.3 ± 0.07 | kcal/mol | Ccr | Carson, Laye, et al., 1993 | ALS |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
19.78 | 298.15 | Carson, Laye, et al., 1993 | DH |
19.6 | 298.15 | Shehatta, 1993 | DH |
19.78 | 298.2 | Low and Moelwyn-Hughes, 1962 | T = 293 to 308 K.; DH |
19.76 | 300. | Harrison and Moelwyn-Hughes, 1957 | T = 243 to 303 K.; DH |
35.40 | 298. | Kurbatov, 1948 | T = -56 to 35°C. Mean Cp five temperatures.; 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
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 315.7 ± 0.2 | K | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 206.7 | K | N/A | Timmermans, 1952 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 208.1 | K | N/A | Timmermans, 1911 | Uncertainty assigned by TRC = 0.4 K; TRC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
7.27 | 243. | A | Stephenson and Malanowski, 1987 | Based on data from 228. to 337. K.; AC |
6.33 | 330. | A | Stephenson and Malanowski, 1987 | Based on data from 315. to 502. K.; AC |
7.43 | 217. | N/A | Wren and Vikis, 1982 | Based on data from 208. to 227. K.; AC |
6.98 | 274. | EB | Boublík and Aim, 1972 | Based on data from 259. to 314. K. See also Kudchadker, Kudchadker, et al., 1979.; AC |
7.27 | 233. | N/A | Stull, 1947 | Based on data from 218. to 315. K.; AC |
6.74 | 288. | N/A | Ewert, 1936 | Based on data from 273. to 307. K.; AC |
6.790 | 315.8 | V | Thompson and Linnett, 1936 | ALS |
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 |
---|---|---|---|---|---|
218. to 315.6 | 4.1497 | 1177.78 | -32.058 | Stull, 1947 | Coefficents calculated by NIST from author's data. |
315.6 to 521. | 4.14326 | 1223.831 | -20.179 | Stull, 1947 | Coefficents calculated by NIST from author's data. |
273.3 to 307.6 | 5.13710 | 1755.986 | 26.111 | Thompson and Linnett, 1936 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.61 ± 0.1 | 191. | VG | Wren and Vikis, 1982 | Based on data from 176. to 227. K.; AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.18 | 206.8 | Wren and Vikis, 1982 | AC |
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
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
MS - José A. Martinho Simões
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: I- + CH3I = (I- • CH3I)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 8.53 ± 0.20 | kcal/mol | N/A | Van Duzor, Wei, et al., 2010 | gas phase; B |
ΔrH° | 7.80 ± 0.20 | kcal/mol | TDAs | Hiraoka, Fujita, et al., 1905 | gas phase; B |
ΔrH° | 8.40 ± 0.50 | kcal/mol | N/A | Arnold, Neumark, et al., 1995 | gas phase; ZEKE data, shift relative to bare I-; B |
ΔrH° | 8.30 ± 0.50 | kcal/mol | PDis | Cyr, Bishea, et al., 1992 | gas phase; B |
ΔrH° | 9.0 ± 2.0 | kcal/mol | TDAs | Dougherty and Roberts, 1974 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 16.4 | cal/mol*K | HPMS | Dougherty and Roberts, 1974 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 2.73 ± 0.20 | kcal/mol | TDAs | Hiraoka, Fujita, et al., 1905 | gas phase; B |
ΔrG° | 4.10 ± 0.30 | kcal/mol | TDAs | Dougherty and Roberts, 1974 | gas phase; B |
By formula: C6H7N+ + CH3I = (C6H7N+ • CH3I)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.7 | 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° | 18. | 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 |
---|---|---|---|---|
4.3 | 299. | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: Cl- + CH3I = (Cl- • CH3I)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.80 ± 0.20 | kcal/mol | TDAs | Dougherty and Roberts, 1974 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 7.3 | cal/mol*K | HPMS | Dougherty and Roberts, 1974 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 7.0 ± 1.3 | kcal/mol | TDAs | Dougherty and Roberts, 1974 | gas phase; B |
By formula: HI + CH3I = CH4 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -12.56 ± 0.13 | kcal/mol | Eqk | Golden, Walsh, et al., 1965 | gas phase; ALS |
ΔrH° | -12.67 ± 0.05 | kcal/mol | Eqk | Goy and Pritchard, 1965 | gas phase; ALS |
ΔrH° | -11.0 ± 1.3 | kcal/mol | Cm | Nichol and Ubbelohde, 1952 | gas phase; ALS |
C12H16Nb (cr) + 2 (cr) = C10H10I2Nb (cr) + 2 (l)
By formula: C12H16Nb (cr) + 2I2 (cr) = C10H10I2Nb (cr) + 2CH3I (l)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -57.91 ± 0.57 | kcal/mol | RSC | Diogo, Simoni, et al., 1993 | The difference between the enthalpies of formation of Nb(Cp)2(I)2 and Nb(Cp)2(Me)2 is calculated as -51.41 ± 0.62 kcal/mol; MS |
C14H22CoN5O4 (solution) + (solution) = C13H19CoIN5O4 (solution) + (solution)
By formula: C14H22CoN5O4 (solution) + I2 (solution) = C13H19CoIN5O4 (solution) + CH3I (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -22.2 ± 0.60 | kcal/mol | RSC | Toscano, Seligson, et al., 1989 | solvent: Bromoform; The enthalpy of solution of Co(py)(dmg)2(Me)(cr) was measured as 2.61 kcal/mol Toscano, Seligson, et al., 1989; MS |
By formula: CH3I2- + 2CH3I = C2H6I3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.00 ± 0.20 | kcal/mol | TDAs | Hiraoka, Fujita, et al., 1905 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1.04 ± 0.20 | kcal/mol | TDAs | Hiraoka, Fujita, et al., 1905 | gas phase; B |
(cr) + (solution) = CH3IMg (solution)
By formula: Mg (cr) + CH3I (solution) = CH3IMg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.4 ± 0.2 | kcal/mol | RSC | Carson and Skinner, 1950 | solvent: Diethyl ether; It was assumed that MeI(l) has a negligible solution enthalpy in ether; MS |
CH2I- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 386.3 ± 4.9 | kcal/mol | G+TS | Ingemann and Nibbering, 1985 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 379.4 ± 4.8 | kcal/mol | IMRB | Ingemann and Nibbering, 1985 | gas phase; B |
By formula: C2H6Hg (l) + 2I2 (cr) = 2CH3I (l) + HgI2 (cr)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -44.1 ± 0.2 | kcal/mol | RSC | Hartley, Pritchard, et al., 1950 | Please also see Pedley and Rylance, 1977 and Cox and Pilcher, 1970, 2.; MS |
(l) + 3 (cr) = GaI3 (cr) + 3 (l)
By formula: C3H9Ga (l) + 3I2 (cr) = GaI3 (cr) + 3CH3I (l)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -47.8 ± 2.0 | kcal/mol | RSC | Fowell and Mortimer, 1958 | Please also see Pedley and Rylance, 1977 and Cox and Pilcher, 1970, 2.; MS |
(l) + 2 (cr) = CH3GaI2 (cr) + 2 (l)
By formula: C3H9Ga (l) + 2I2 (cr) = CH3GaI2 (cr) + 2CH3I (l)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -37.9 ± 1.0 | kcal/mol | RSC | Fowell and Mortimer, 1958 | Please also see Pedley and Rylance, 1977 and Cox and Pilcher, 1970, 2.; MS |
C16H34P2Ru (solution) + (solution) = C16H33IP2Ru (solution) + (solution)
By formula: C16H34P2Ru (solution) + CH3I (solution) = C16H33IP2Ru (solution) + CH4 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -45.00 ± 0.69 | kcal/mol | RSC | Luo, Li, et al., 1995 | solvent: Tetrahydrofuran; MS |
C22H36Zr (solution) + 2 (solution) = C20H30I2Zr (solution) + 2 (solution)
By formula: C22H36Zr (solution) + 2I2 (solution) = C20H30I2Zr (solution) + 2CH3I (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -70.00 ± 0.60 | kcal/mol | RSC | Schock and Marks, 1988 | solvent: Toluene; MS |
C8H5MoNaO3 (solution) + (l) = C9H8MoO3 (solution) + (cr)
By formula: C8H5MoNaO3 (solution) + CH3I (l) = C9H8MoO3 (solution) + INa (cr)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -7.70 ± 0.31 | kcal/mol | RSC | Nolan, López de la Vega, et al., 1986 | solvent: Tetrahydrofuran; MS |
C12H16Zr (solution) + 2 (solution) = C10H10I2Zr (solution) + 2 (solution)
By formula: C12H16Zr (solution) + 2I2 (solution) = C10H10I2Zr (solution) + 2CH3I (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -69.60 ± 0.60 | kcal/mol | RSC | Schock and Marks, 1988 | solvent: Toluene; MS |
C22H36Hf (solution) + 2 (solution) = C20H30HfI2 (solution) + 2 (solution)
By formula: C22H36Hf (solution) + 2I2 (solution) = C20H30HfI2 (solution) + 2CH3I (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -63.41 ± 0.79 | kcal/mol | RSC | Schock and Marks, 1988 | solvent: Toluene; MS |
By formula: H2 + 2CH3I = 2CH4 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -30.0 ± 0.6 | kcal/mol | Chyd | Carson, Carter, et al., 1961 | liquid phase; solvent: Ether; ALS |
By formula: CH4 + CH2I2 = 2CH3I
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4.7 ± 1.0 | kcal/mol | Eqk | Furuyama, Golden, et al., 1968 | 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 |
---|---|---|---|---|
0.14 | 4300. | M | N/A | |
0.35 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.19 | 3800. | M | N/A | |
0.18 | V | N/A | ||
0.17 | C | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
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) | 9.54 ± 0.02 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 165.3 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 159.1 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Electron affinity determinations
EA (eV) | Method | Reference | Comment |
---|---|---|---|
0.110 ± 0.020 | LPES | Kim, Kelley, et al., 1999 | B |
0.30 ± 0.20 | NBIE | Moutinho, Aten, et al., 1974 | Stated electron affinity is the Vertical Detachment Energy; B |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.54 ± 0.05 | EI | Holmes and Lossing, 1991 | LL |
9.54 | PE | Carlson, Gerard, et al., 1988 | LL |
10.86 | S | Baig, Connerade, et al., 1982 | LBLHLM |
9.54 | PE | Kimura, Katsumata, et al., 1981 | LLK |
9.538 | EQ | Lias and Ausloos, 1978 | LLK |
9.54 | PIPECO | Mintz and Baer, 1976 | LLK |
9.53 ± 0.01 | PI | Tsai, Baer, et al., 1975 | LLK |
9.538 | S | Hochmann, Templet, et al., 1975 | LLK |
9.54 | PE | Boschi and Salahub, 1974 | LLK |
9.48 ± 0.03 | EI | Johnstone and Mellon, 1972 | LLK |
9.538 | S | Boschi and Salahub, 1972 | LLK |
9.52 | PE | Brogli and Heilbronner, 1971 | LLK |
10.14 | PE | Brogli and Heilbronner, 1971 | LLK |
9.50 | PE | Ragle, Stenhouse, et al., 1970 | RDSH |
9.54 | PE | Potts, Lempka, et al., 1970 | RDSH |
9.534 ± 0.005 | TE | Baer, Peatman, et al., 1969 | RDSH |
9.538 ± 0.003 | S | Price, 1936 | RDSH |
9.53 | PE | Utsunomiya, Kobayashi, et al., 1980 | Vertical value; LLK |
9.9 | PE | Dromey and Peel, 1974 | Vertical value; LLK |
9.51 | PE | Uehara, Saito, et al., 1973 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH+ | 21.2 ± 0.2 | ? | EI | Reed and Snedden, 1956 | RDSH |
CH2+ | 14.6 ± 0.2 | HI | EI | Tsuda and Hamill, 1964 | RDSH |
CH2I+ | 12.78 | H | EI | Holmes, Lossing, et al., 1988 | LL |
CH2I+ | 12.08 ± 0.09 | H | EI | Martin, Lampe, et al., 1966 | RDSH |
CH3+ | 12.18 | I | PI | Traeger and McLoughlin, 1981 | LLK |
CH3+ | 12.24 ± 0.01 | I | PIPECO | Mintz and Baer, 1976 | LLK |
CH3+ | 12.25 ± 0.03 | I | PI | Tsai, Baer, et al., 1975 | LLK |
CH3+ | 12.07 ± 0.07 | I | EI | Johnstone and Mellon, 1972 | LLK |
CH3+ | 12.260 ± 0.013 | I | PI | Nicholson, 1970 | RDSH |
CH3+ | 12.22 | I | EI | Lossing and Semeluk, 1970 | RDSH |
I+ | 12.9 ± 0.05 | CH3 | EI | Tsuda, Melton, et al., 1964 | RDSH |
De-protonation reactions
CH2I- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 386.3 ± 4.9 | kcal/mol | G+TS | Ingemann and Nibbering, 1985 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 379.4 ± 4.8 | kcal/mol | IMRB | Ingemann and Nibbering, 1985 | gas phase; B |
IR Spectrum
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, Mass spectrum (electron ionization), References, Notes
Data compiled by: Coblentz Society, Inc.
- GAS (200 mmHg DILUTED TO A TOTAL PRESSURE OF 600 mmHg WITH N2); DOW KBr FOREPRISM; DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 cm-1 resolution
- LIQUID; Not specified, most likely a prism, grating, or hybrid spectrometer.; DIGITIZED BY NIST FROM HARD COPY; 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, Reaction thermochemistry 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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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 | 118703 |
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), Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Golden, Walsh, et al., 1965
Golden, D.M.; Walsh, R.; Benson, S.W.,
The thermochemistry of the gas phase equilibrium I2 + CH4 «=» CH3I + HI and the heat of formation of the methyl radical,
J. Am. Chem. Soc., 1965, 87, 4053-4057. [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]
Goy and Pritchard, 1965
Goy, C.A.; Pritchard, H.O.,
Kinetics and thermodynamics of the reaction between iodine and methane and the heat of formation of methyl iodide,
J. Phys. Chem., 1965, 69, 3040-3041. [all data]
Carson, Carter, et al., 1961
Carson, A.S.; Carter, W.; Pedley, J.B.,
The thermochemistry of reductions caused by lithium aluminium hydride I. The C-I bond dissociation energy in CH3I,
Proc. Roy. Soc. London A, 1961, 260, 550-557. [all data]
Carson, Laye, et al., 1993
Carson, A.S.; Laye, P.G.; Pedley, J.B.; Welsby, A.M.,
The enthalpies of formation iodomethane, diiodomethane, triiodomethane, and tetraiodomethane by rotating combustion calorimetry,
J. Chem. Thermodyn., 1993, 25, 261-269. [all data]
Shehatta, 1993
Shehatta, I.,
Heat capacity at constant pressure of some halogen compounds,
Thermochim. Acta, 1993, 213, 1-10. [all data]
Low and Moelwyn-Hughes, 1962
Low, D.I.R.; Moelwyn-Hughes, E.A.,
The heat capacities of acetone, methyl iodide and mixtures thereof in the liquid state,
Proc. Roy. Soc. (London), 1962, A267, 384-394. [all data]
Harrison and Moelwyn-Hughes, 1957
Harrison, D.; Moelwyn-Hughes, E.A.,
The heat capacities of certain liquids,
Proc. Roy. Soc. (London), 1957, A239, 230-246. [all data]
Kurbatov, 1948
Kurbatov, V.Ya.,
Heat capacity of liquids. 2. Heat capacity and the temperature dependence of heat capacity from halogen derivatives of acylic hydrocarbons,
Zh. Obshch. Kim., 1948, 18, 372-389. [all data]
Timmermans, 1952
Timmermans, J.,
Freezing points of organic compounds. VVI New determinations.,
Bull. Soc. Chim. Belg., 1952, 61, 393. [all data]
Timmermans, 1911
Timmermans, J.,
Researches on the freezing point of organic liquid compounds,
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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 EA Electron affinity IE (evaluated) Recommended ionization energy T Temperature Tboil Boiling point Tfus Fusion (melting) point 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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