Chemical Properties of Methane, nitro- (CAS 75-52-5)

InChI

InChI=1S/CH3NO2/c1-2(3)4/h1H3

InChI Key

LYGJENNIWJXYER-UHFFFAOYSA-N

Formula

CH3NO2

SMILES

C[N+](=O)[O-]

Molecular Weight¹

61.04

CAS

75-52-5

Other Names

• CH3NO2
• NM
• NSC 428
• Nitrocarbol
• Nitrometan
• Nitromethane
• UN 1261
• nitromethane [NM]

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• EA : Electron affinity (eV).
• LFL : Lower Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3100		KDB
PAff	754.60	kJ/mol	NIST
Tig	691.48	K	KDB
BasG	721.60	kJ/mol	NIST
ΔcH°liquid	[-733.25; -703.00]	kJ/mol
ΔcH°liquid	-709.60 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-703.00 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-709.15 ± 0.59	kJ/mol	NIST
ΔcH°liquid	-733.25 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-709.20	kJ/mol	NIST
μ	3.10	debye	KDB
EA	[0.01; 0.96]	eV
EA	0.17 ± 0.01	eV	NIST
EA	0.26 ± 0.08	eV	NIST
EA	0.01	eV	NIST
EA	0.50 ± 0.02	eV	NIST
EA	0.49 ± 0.11	eV	NIST
EA	0.45 ± 0.05	eV	NIST
EA	0.44 ± 0.20	eV	NIST
EA	Outlier 0.96 ± 0.01	eV	NIST
LFL	7.30	% in Air	KDB
Tflash,cc	316.48	K	KDB
Tflash,oc	308.15	K	KDB
ΔfG°	-6.95	kJ/mol	KDB
Rg	2.3060		KDB
ΔfH°gas	[-81.00; -74.78]	kJ/mol
ΔfH°gas	-74.78	kJ/mol	KDB
ΔfH°gas	-81.00 ± 1.00	kJ/mol	NIST
ΔfH°liquid	[-113.10; -89.04]	kJ/mol
ΔfH°liquid	-113.00 ± 0.40	kJ/mol	NIST
ΔfH°liquid	-113.10 ± 0.63	kJ/mol	NIST
ΔfH°liquid	-89.04 ± 0.75	kJ/mol	NIST
ΔfusH°	9.71	kJ/mol	Joback Calculated Property
ΔvapH°	[34.50; 38.37]	kJ/mol
ΔvapH°	38.36	kJ/mol	NIST
ΔvapH°	37.20	kJ/mol	NIST
ΔvapH°	38.37	kJ/mol	NIST
ΔvapH°	38.00 ± 0.40	kJ/mol	NIST
ΔvapH°	38.00 ± 0.40	kJ/mol	NIST
ΔvapH°	38.30 ± 0.10	kJ/mol	NIST
ΔvapH°	Outlier 34.50 ± 0.08	kJ/mol	NIST
IE	[10.70; 11.80]	eV
IE	11.08 ± 0.04	eV	NIST
IE	11.07	eV	NIST
IE	11.10 ± 0.05	eV	NIST
IE	Outlier 10.70	eV	NIST
IE	11.12	eV	NIST
IE	11.05	eV	NIST
IE	11.28 ± 0.08	eV	NIST
IE	11.28	eV	NIST
IE	11.10	eV	NIST
IE	11.28 ± 0.08	eV	NIST
IE	11.07 ± 0.01	eV	NIST
IE	11.04 ± 0.02	eV	NIST
IE	11.23 ± 0.01	eV	NIST
IE	11.13 ± 0.01	eV	NIST
IE	11.08 ± 0.03	eV	NIST
IE	11.29	eV	NIST
IE	11.47	eV	NIST
IE	11.31	eV	NIST
IE	Outlier 11.80	eV	NIST
IE	11.29	eV	NIST
IE	11.31 ± 0.01	eV	NIST
log10WS	[0.26; 0.26]
log10WS	0.26		Aq. Solubility Prediction
log10WS	0.26		Estimated Solubility
logPoct/wat	-0.107		Crippen Calculated Property
McVol	42.370	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
NFPA Safety	4		KDB
Pc	[5870.00; 6310.00]	kPa
Pc	5870.00	kPa	KDB
Pc	5870.00 ± 58.65	kPa	NIST
Pc	6310.00 ± 103.42	kPa	NIST
ρc	352.20 ± 3.05	kg/m3	NIST
Inp	[487.00; 565.00]
Inp	527.85		NIST
Inp	528.16		NIST
Inp	528.60		NIST
Inp	531.15		NIST
Inp	530.05		NIST
Inp	529.26		NIST
Inp	528.66		NIST
Inp	528.15		NIST
Inp	527.88		NIST
Inp	527.75		NIST
Inp	526.13		NIST
Inp	556.00		NIST
Inp	500.00		NIST
Inp	500.00		NIST
Inp	536.00		NIST
Inp	565.00		NIST
Inp	565.00		NIST
Inp	565.00		NIST
Inp	512.00		NIST
Inp	543.60		NIST
Inp	531.00		NIST
Inp	521.00		NIST
Inp	Outlier 487.00		NIST
Inp	526.00		NIST
Inp	531.00		NIST
Inp	521.00		NIST
Inp	526.00		NIST
Inp	565.00		NIST
Inp	536.00		NIST
Inp	565.00		NIST
Inp	531.00		NIST
I	[1154.00; 1190.20]
I	1187.80		NIST
I	1188.50		NIST
I	1190.20		NIST
I	1178.50		NIST
I	1179.20		NIST
I	1180.60		NIST
I	1182.90		NIST
I	1184.70		NIST
I	1172.00		NIST
I	1159.00		NIST
I	1160.90		NIST
I	1177.00		NIST
I	1177.00		NIST
I	Outlier 1154.00		NIST
I	1159.00		NIST
I	1187.80		NIST
I	1180.60		NIST
S°liquid	171.75	J/mol×K	NIST
Tboil	[373.13; 374.85]	K
Tboil	374.34	K	KDB
Tboil	373.35 ± 0.50	K	NIST
Tboil	373.35 ± 0.50	K	NIST
Tboil	374.40	K	NIST
Tboil	374.43 ± 0.30	K	NIST
Tboil	374.17 ± 0.25	K	NIST
Tboil	374.35 ± 0.05	K	NIST
Tboil	374.85 ± 0.30	K	NIST
Tboil	374.22 ± 0.08	K	NIST
Tboil	Outlier 373.13 ± 0.07	K	NIST
Tboil	374.40 ± 0.50	K	NIST
Tboil	374.15 ± 1.50	K	NIST
Tboil	374.40 ± 0.50	K	NIST
Tboil	374.25 ± 0.30	K	NIST
Tboil	374.30 ± 0.50	K	NIST
Tboil	374.17 ± 0.30	K	NIST
Tboil	374.15 ± 1.00	K	NIST
Tboil	374.15 ± 2.00	K	NIST
Tc	[588.00; 588.00]	K
Tc	588.00	K	KDB
Tc	588.00	K	NIST
Tc	588.00 ± 3.00	K	NIST
Tfus	[243.11; 244.60]	K
Tfus	244.32	K	Aq. Solubility Prediction
Tfus	244.60	K	KDB
Tfus	243.36	K	Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus	244.60 ± 0.05	K	NIST
Tfus	244.55 ± 0.40	K	NIST
Tfus	243.11 ± 0.05	K	NIST
Tfus	244.00 ± 2.00	K	NIST
Tfus	243.95 ± 0.30	K	NIST
Ttriple	244.77 ± 0.02	K	NIST
Vc	0.173	m3/kmol	KDB
Zc	0.2077160		KDB
Zra	0.23		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[67.43; 90.47]	J/mol×K	[374.12; 587.84]
Cp,gas	67.43	J/mol×K	374.12	Joback Calculated Property
Cp,gas	71.78	J/mol×K	409.74	Joback Calculated Property
Cp,gas	75.92	J/mol×K	445.36	Joback Calculated Property
Cp,gas	79.86	J/mol×K	480.98	Joback Calculated Property
Cp,gas	83.59	J/mol×K	516.60	Joback Calculated Property
Cp,gas	87.12	J/mol×K	552.22	Joback Calculated Property
Cp,gas	90.47	J/mol×K	587.84	Joback Calculated Property
Cp,liquid	[100.00; 108.80]	J/mol×K	[293.15; 318.15]
Cp,liquid	106.60	J/mol×K	293.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
Cp,liquid	100.00	J/mol×K	298.00	NIST
Cp,liquid	106.90	J/mol×K	298.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
Cp,liquid	105.98	J/mol×K	298.15	NIST
Cp,liquid	107.30	J/mol×K	303.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
Cp,liquid	106.22	J/mol×K	308.00	NIST
Cp,liquid	107.70	J/mol×K	308.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
Cp,liquid	108.80	J/mol×K	313.00	NIST
Cp,liquid	108.20	J/mol×K	313.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
Cp,liquid	108.60	J/mol×K	318.15	Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
ΔfusH	[9.70; 9.70]	kJ/mol	[244.77; 244.80]
ΔfusH	9.70	kJ/mol	244.77	NIST
ΔfusH	9.70	kJ/mol	244.80	NIST
ΔfusH	9.70	kJ/mol	244.80	NIST
ΔvapH	[33.99; 38.27]	kJ/mol	[298.15; 440.50]
ΔvapH	38.27	kJ/mol	298.15	NIST
ΔvapH	37.20 ± 0.10	kJ/mol	318.00	NIST
ΔvapH	36.30 ± 0.10	kJ/mol	335.00	NIST
ΔvapH	35.20 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	36.80	kJ/mol	369.00	NIST
ΔvapH	34.41	kJ/mol	374.00	KDB
ΔvapH	34.00 ± 0.10	kJ/mol	374.00	NIST
ΔvapH	33.99	kJ/mol	374.40	NIST
ΔvapH	35.20	kJ/mol	440.50	NIST
ν	[0.0000005; 0.0000006]	m2/s	[293.15; 308.15]
ν	0.0000006	m2/s	293.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000006	m2/s	295.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000006	m2/s	298.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000005	m2/s	300.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000005	m2/s	303.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000005	m2/s	305.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν	0.0000005	m2/s	308.15	Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
n0	[1.37930; 1.37990]		[298.15; 298.15]
n0	1.37956		298.15	Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
n0	1.37960		298.15	Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
n0	1.37990		298.15	Physico-chemical studies of sodium tetraphenylborate and tetrabutylammonium tetraphenylborate in pure nitrobenzene and nitromethane and their binaries probed by conductometry, refractometry and FT-IR spectroscopy
n0	1.37930		298.15	Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
n0	1.37940		298.15	Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K
ρl	[1103.39; 1158.25]	kg/m3	[278.15; 318.15]
ρl	1158.25	kg/m3	278.15	Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
ρl	1144.75	kg/m3	288.15	Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
ρl	1138.00	kg/m3	293.00	KDB
ρl	1140.20	kg/m3	293.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ρl	1130.90	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1131.18	kg/m3	298.15	Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
ρl	1130.15	kg/m3	298.15	Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
ρl	1131.10	kg/m3	298.15	Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
ρl	1130.15	kg/m3	298.15	Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
ρl	1130.90	kg/m3	298.15	Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
ρl	1130.86	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1130.76	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1133.40	kg/m3	298.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ρl	1130.91	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1130.95	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1126.60	kg/m3	303.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ρl	1119.70	kg/m3	308.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ρl	1117.28	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1117.23	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1117.29	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1117.32	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1117.53	kg/m3	308.15	Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
ρl	1117.24	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1117.14	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1112.90	kg/m3	313.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ρl	1103.50	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.48	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.39	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.57	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.53	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.55	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1103.79	kg/m3	318.15	Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
ρl	1106.00	kg/m3	318.15	Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
ΔfusS	39.64	J/mol×K	244.77	NIST
csound,fluid	[1242.39; 1321.74]	m/s	[298.15; 318.15]
csound,fluid	1321.18	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.33	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.74	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.16	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.50	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.20	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.49	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.62	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1321.26	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1281.77	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1281.87	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1281.90	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1281.78	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1282.03	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1282.12	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1281.75	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.39	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.46	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.50	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.49	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.76	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.45	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.47	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1242.60	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
γ	0.04	N/m	293.20	KDB
ΔvapS	128.36	J/mol×K	298.15	NIST

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	1130.15
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.14; 6410.96]	kPa	[244.60; 588.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.53705e+01
Coefficient B			-3.66507e+03
Coefficient C			-3.32310e+01
Temperature range, min.			244.60
Temperature range, max.			588.15
Pvap	0.14	kPa	244.60	Calculated Property
Pvap	1.98	kPa	282.77	Calculated Property
Pvap	13.90	kPa	320.94	Calculated Property
Pvap	61.80	kPa	359.12	Calculated Property
Pvap	200.98	kPa	397.29	Calculated Property
Pvap	522.48	kPa	435.46	Calculated Property
Pvap	1150.98	kPa	473.63	Calculated Property
Pvap	2235.35	kPa	511.81	Calculated Property
Pvap	3935.82	kPa	549.98	Calculated Property
Pvap	6410.96	kPa	588.15	Calculated Property
Pvap	[0.14; 6066.19]	kPa	[244.60; 588.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.31812e+01
Coefficient B			-7.21717e+03
Coefficient C			-1.02078e+01
Coefficient D			8.36912e-06
Temperature range, min.			244.60
Temperature range, max.			588.15
Pvap	0.14	kPa	244.60	Calculated Property
Pvap	2.03	kPa	282.77	Calculated Property
Pvap	14.07	kPa	320.94	Calculated Property
Pvap	60.62	kPa	359.12	Calculated Property
Pvap	189.81	kPa	397.29	Calculated Property
Pvap	477.23	kPa	435.46	Calculated Property
Pvap	1029.09	kPa	473.63	Calculated Property
Pvap	1991.26	kPa	511.81	Calculated Property
Pvap	3569.52	kPa	549.98	Calculated Property
Pvap	6066.19	kPa	588.15	Calculated Property

Similar Compounds

Find more compounds similar to Methane, nitro-.

Mixtures

• Tetrabutylammonium hexafluorophosphate + Methane, nitro-
• Pentane, 1-chloro- + Methane, nitro-
• n-Butyl ether + Methane, nitro-
• Hexane, 1-ethoxy- + Methane, nitro-
• Pentane, 1-propoxy- + Methane, nitro-
• Methane, nitro- + Ethane, 1,1,2,2-tetrachloro-
• Ethane, 1,1,1-trichloro- + Methane, nitro-
• Trichloromethane + Methane, nitro-
• Ethane, 1,2-dichloro- + Methane, nitro-
• Methane, nitro- + Propane, 1,3-dichloro-
• Butane, 1,4-dichloro- + Methane, nitro-
• Butane, 1-chloro- + Methane, nitro-
• Methane, nitro- + Water
• Benzene, nitro- + Methane, nitro-
• Acetic acid, pentyl ester + Methane, nitro-
• Methane, nitro- + 3-Pentanol
• 1-Pentanol + Methane, nitro-
• Methane, nitro- + Tetrabutylammonium tetrafluoroborate
• Carbon dioxide + Methane, nitro-

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Isothermal vapour liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
• Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
• Liquid-liquid equilibrium in binary systems of isomeric C8 aliphatic monoethers with nitromethane
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
• Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
• Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
• Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Physico-chemical studies of sodium tetraphenylborate and tetrabutylammonium tetraphenylborate in pure nitrobenzene and nitromethane and their binaries probed by conductometry, refractometry and FT-IR spectroscopy
• Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Enthalpies of formation of nitromethane and nitrobenzene: New experiments vs. quantum chemical calculations
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
• Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
• Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Role of Anions (Tetrafluoroborate, Perchlorate) of Tetrabutylammonium Salts in Determining Solvation Effects Prevailing in Industrially Essential Solvents Probed by Conductance and FT-IR Spectra
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
• Densities and Excess Enthalpies for Ionic Liquids + Ethanol or + Nitromethane
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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