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
• Nitrometan
• UN 1261
• nitrocarbol
• nitromethane
• nitromethane [NM]

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• α_p : Isobaric thermal expansion coefficient (1/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).
• η : Dynamic viscosity (Pa×s).
• 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_triple : Triple Point 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_p : 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).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.3100; 0.3480]
ω	0.3480		ChemSep v8.3 pure component data Compiled value
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; 3.45]	debye
μ	3.45	debye	ChemSep v8.3 pure component data Compiled value
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; -6.94]	kJ/mol
ΔfG°	-6.94	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-6.95	kJ/mol	KDB
Rg	2.3060		KDB
ΔfH°gas	[-81.00; -74.78]	kJ/mol
ΔfH°gas	-74.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
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	ChemSep v8.3 pure component data Compiled value
Pc	5870.00	kPa	KDB
Pc	5870.00 ± 58.65	kPa	NIST
Pc	6310.00 ± 103.42	kPa	NIST
Ptriple	0.15	kPa	ChemSep v8.3 pure component data Compiled value
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
Ip	[1154.00; 1190.20]
Ip	1187.80		NIST
Ip	1188.50		NIST
Ip	1190.20		NIST
Ip	1178.50		NIST
Ip	1179.20		NIST
Ip	1180.60		NIST
Ip	1182.90		NIST
Ip	1184.70		NIST
Ip	1172.00		NIST
Ip	1159.00		NIST
Ip	1160.90		NIST
Ip	1177.00		NIST
Ip	1177.00		NIST
Ip	Outlier 1154.00		NIST
Ip	1159.00		NIST
Ip	1187.80		NIST
Ip	1180.60		NIST
S°liquid	171.75	J/mol×K	NIST
Tboil	[373.13; 374.85]	K
Tboil	374.35	K	ChemSep v8.3 pure component data Compiled value
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	ChemSep v8.3 pure component data Compiled value
Tc	588.00	K	KDB
Tc	588.00	K	NIST
Tc	588.00 ± 3.00	K	NIST
Tfus	[243.11; 244.60]	K
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	K	ChemSep v8.3 pure component data Compiled value
Tfus	244.60	K	KDB
Tfus	244.32	K	Aq. Solubility Prediction
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	[244.60; 244.77]	K
Ttriple	244.60	K	ChemSep v8.3 pure component data Compiled value
Ttriple	244.77 ± 0.02	K	NIST
Ttriple	244.77 ± 0.02	K	NIST
UQi	1.87		ChemSep v8.3 pure component data Compiled value
URi	2.01		ChemSep v8.3 pure component data Compiled value
Vc	[0.173; 0.173]	m3/kmol
Vc	0.173	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.173	m3/kmol	KDB
Zc	[0.2077160; 0.2080000]
Zc	0.2080000		ChemSep v8.3 pure component data Compiled value
Zc	0.2077160		KDB
Zra	[0.22; 0.23]
Zra	0.22		ChemSep v8.3 pure component data Compiled value
Zra	0.23		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
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	244.77	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	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 Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
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	1130.15	kg/m3	298.15	Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
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	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	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	1130.91	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	1130.76	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	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	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	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	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	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	1117.53	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	1117.32	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	1117.24	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	1117.29	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	1117.14	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	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	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	1103.39	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	1103.48	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	1103.50	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	1103.57	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	1103.79	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	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	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
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
ΔfusS	[39.64; 39.64]	J/mol×K	[244.77; 244.77]
ΔfusS	39.64	J/mol×K	244.77	NIST
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; 128.36]	J/mol×K	[298.15; 298.15]
ΔvapS	128.36	J/mol×K	298.15	NIST
ΔvapS	128.36	J/mol×K	298.15	NIST

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Mass density, kg/m3 (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0012
278.15	10000.00	0.0011
278.15	15000.00	0.0011
278.15	20000.00	0.0011
278.15	25000.00	0.0011
278.15	30000.00	0.0011
278.15	35000.00	0.0010
278.15	40000.00	0.0010
278.15	45000.00	0.0010
278.15	50000.00	0.0010
278.15	55000.00	0.0010
288.15	5000.00	0.0012
288.15	10000.00	0.0012
288.15	15000.00	0.0011
288.15	20000.00	0.0011
288.15	25000.00	0.0011
288.15	30000.00	0.0011
288.15	35000.00	0.0011
288.15	40000.00	0.0010
288.15	45000.00	0.0010
288.15	50000.00	0.0010
288.15	55000.00	0.0010
298.15	5000.00	0.0012
298.15	10000.00	0.0012
298.15	15000.00	0.0012
298.15	20000.00	0.0011
298.15	25000.00	0.0011
298.15	30000.00	0.0011
298.15	35000.00	0.0011
298.15	40000.00	0.0010
298.15	45000.00	0.0010
298.15	50000.00	0.0010
298.15	55000.00	0.0010
308.15	5000.00	0.0012
308.15	10000.00	0.0012
308.15	15000.00	0.0012
308.15	20000.00	0.0011
308.15	25000.00	0.0011
308.15	30000.00	0.0011
308.15	35000.00	0.0011
308.15	40000.00	0.0011
308.15	45000.00	0.0010
308.15	50000.00	0.0010
308.15	55000.00	0.0010
318.15	5000.00	0.0013
318.15	10000.00	0.0012
318.15	15000.00	0.0012
318.15	20000.00	0.0012
318.15	25000.00	0.0011
318.15	30000.00	0.0011
318.15	35000.00	0.0011
318.15	40000.00	0.0011
318.15	45000.00	0.0010
318.15	50000.00	0.0010
318.15	55000.00	0.0010
328.15	5000.00	0.0013
328.15	10000.00	0.0013
328.15	15000.00	0.0012
328.15	20000.00	0.0012
328.15	25000.00	0.0011
328.15	30000.00	0.0011
328.15	35000.00	0.0011
328.15	40000.00	0.0011
328.15	45000.00	0.0010
328.15	50000.00	0.0010
328.15	55000.00	0.0010
338.15	5000.00	0.0013
338.15	10000.00	0.0013
338.15	15000.00	0.0012
338.15	20000.00	0.0012
338.15	25000.00	0.0012
338.15	30000.00	0.0011
338.15	35000.00	0.0011
338.15	40000.00	0.0011
338.15	45000.00	0.0011
338.15	50000.00	0.0010
338.15	55000.00	0.0010
348.15	5000.00	0.0014
348.15	10000.00	0.0013
348.15	15000.00	0.0013
348.15	20000.00	0.0012
348.15	25000.00	0.0012
348.15	30000.00	0.0011
348.15	35000.00	0.0011
348.15	40000.00	0.0011
348.15	45000.00	0.0011
348.15	50000.00	0.0010
348.15	55000.00	0.0010
Reference

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
Cp,gas	[41.10; 132.80]	J/mol×K	[150.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.86810e+01
Coefficient B			-6.15840e+02
Coefficient C			4.98724e+00
Coefficient D			2.31180e-05
Coefficient E			-2.96770e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	41.10	J/mol×K	150.00	Calculated Property
Cp,gas	57.57	J/mol×K	300.00	Calculated Property
Cp,gas	76.13	J/mol×K	450.00	Calculated Property
Cp,gas	91.35	J/mol×K	600.00	Calculated Property
Cp,gas	103.19	J/mol×K	750.00	Calculated Property
Cp,gas	112.36	J/mol×K	900.00	Calculated Property
Cp,gas	119.51	J/mol×K	1050.00	Calculated Property
Cp,gas	125.09	J/mol×K	1200.00	Calculated Property
Cp,gas	129.44	J/mol×K	1350.00	Calculated Property
Cp,gas	132.80	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[103.90; 129.53]	J/mol×K	[244.60; 473.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			8.05880e+01
Coefficient B			3.45480e+02
Coefficient C			-1.50255e-01
Coefficient D			8.47940e-03
Coefficient E			-3.13260e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			244.60
Temperature range, max.			473.15
Cp,liquid	103.90	J/mol×K	244.60	Calculated Property
Cp,liquid	104.89	J/mol×K	269.99	Calculated Property
Cp,liquid	106.40	J/mol×K	295.39	Calculated Property
Cp,liquid	108.37	J/mol×K	320.78	Calculated Property
Cp,liquid	110.78	J/mol×K	346.18	Calculated Property
Cp,liquid	113.63	J/mol×K	371.57	Calculated Property
Cp,liquid	116.91	J/mol×K	396.97	Calculated Property
Cp,liquid	120.64	J/mol×K	422.36	Calculated Property
Cp,liquid	124.84	J/mol×K	447.76	Calculated Property
Cp,liquid	129.53	J/mol×K	473.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0013447; 0.0001945]	Pa×s	[244.60; 454.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.04110e+01
Coefficient B			1.04760e+03
Coefficient C			-9.54450e-02
Coefficient D			6.91980e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			244.60
Temperature range, max.			454.00
η	0.0013447	Pa×s	244.60	Calculated Property
η	0.0009266	Pa×s	267.87	Calculated Property
η	0.0006786	Pa×s	291.13	Calculated Property
η	0.0005212	Pa×s	314.40	Calculated Property
η	0.0004158	Pa×s	337.67	Calculated Property
η	0.0003421	Pa×s	360.93	Calculated Property
η	0.0002887	Pa×s	384.20	Calculated Property
η	0.0002488	Pa×s	407.47	Calculated Property
η	0.0002184	Pa×s	430.73	Calculated Property
η	0.0001945	Pa×s	454.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[40.54; 18.27]	kJ/mol	[244.60; 570.07]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			4.16100e+01
Coefficient B			-6.62124e-01
Coefficient C			2.67118e+00
Coefficient D			-2.70281e+00
Coefficient E			9.31262e-01
Critical temperature, Tc (K)			5.88000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			244.60
Temperature range, max.			570.07
ΔvapH	40.54	kJ/mol	244.60	Calculated Property
ΔvapH	39.03	kJ/mol	280.76	Calculated Property
ΔvapH	37.39	kJ/mol	316.93	Calculated Property
ΔvapH	35.64	kJ/mol	353.09	Calculated Property
ΔvapH	33.79	kJ/mol	389.25	Calculated Property
ΔvapH	31.83	kJ/mol	425.42	Calculated Property
ΔvapH	29.68	kJ/mol	461.58	Calculated Property
ΔvapH	27.18	kJ/mol	497.74	Calculated Property
ΔvapH	23.92	kJ/mol	533.91	Calculated Property
ΔvapH	18.27	kJ/mol	570.07	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.14; 6410.96]	kPa	[244.60; 588.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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; 6121.98]	kPa	[244.15; 588.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			8.63622e+01
Coefficient B			-7.34510e+03
Coefficient C			-1.06890e+01
Coefficient D			8.69980e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			244.15
Temperature range, max.			588.15
Pvap	0.14	kPa	244.15	Calculated Property
Pvap	2.06	kPa	282.37	Calculated Property
Pvap	14.41	kPa	320.59	Calculated Property
Pvap	62.22	kPa	358.82	Calculated Property
Pvap	194.54	kPa	397.04	Calculated Property
Pvap	487.60	kPa	435.26	Calculated Property
Pvap	1047.58	kPa	473.48	Calculated Property
Pvap	2019.83	kPa	511.71	Calculated Property
Pvap	3609.95	kPa	549.93	Calculated Property
Pvap	6121.98	kPa	588.15	Calculated Property
Pvap	[0.14; 6066.19]	kPa	[244.60; 588.15]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.31812e+01
Coefficient B			-7.21717e+03
Coefficient C			-1.02078e+01
Coefficient D			8.36912e-06
Coefficient E			0.00000e+00
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
Pvap	[236.42; 1091.10]	kPa	[405.00; 476.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40769e+01
Coefficient B			-2.83120e+03
Coefficient C			-7.62210e+01
Reference			Berman and West, 1967
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			405.00
Temperature range, max.			476.00
Pvap	236.42	kPa	405.00	Calculated Property
Pvap	289.28	kPa	412.89	Calculated Property
Pvap	350.70	kPa	420.78	Calculated Property
Pvap	421.51	kPa	428.67	Calculated Property
Pvap	502.56	kPa	436.56	Calculated Property
Pvap	594.69	kPa	444.44	Calculated Property
Pvap	698.77	kPa	452.33	Calculated Property
Pvap	815.63	kPa	460.22	Calculated Property
Pvap	946.13	kPa	468.11	Calculated Property
Pvap	1091.10	kPa	476.00	Calculated Property
Pvap	[19.92; 270.39]	kPa	[328.86; 409.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47490e+01
Coefficient B			-3.32999e+03
Coefficient C			-4.56330e+01
Reference			McCullough, Scott, et al., 1954
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			328.86
Temperature range, max.			409.60
Pvap	19.92	kPa	328.86	Calculated Property
Pvap	28.58	kPa	337.83	Calculated Property
Pvap	40.13	kPa	346.80	Calculated Property
Pvap	55.26	kPa	355.77	Calculated Property
Pvap	74.73	kPa	364.74	Calculated Property
Pvap	99.40	kPa	373.72	Calculated Property
Pvap	130.23	kPa	382.69	Calculated Property
Pvap	168.25	kPa	391.66	Calculated Property
Pvap	214.58	kPa	400.63	Calculated Property
Pvap	270.39	kPa	409.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1197.15; 355.18]	kg/m3	[244.60; 588.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.44383e+01
Coefficient B			2.24760e-01
Coefficient C			5.88160e+02
Coefficient D			2.78700e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			244.60
Temperature range, max.			588.15
ρl	1197.15	kg/m3	244.60	Calculated Property
ρl	1148.49	kg/m3	282.77	Calculated Property
ρl	1097.48	kg/m3	320.94	Calculated Property
ρl	1043.56	kg/m3	359.12	Calculated Property
ρl	985.88	kg/m3	397.29	Calculated Property
ρl	923.13	kg/m3	435.46	Calculated Property
ρl	853.03	kg/m3	473.63	Calculated Property
ρl	771.02	kg/m3	511.81	Calculated Property
ρl	664.67	kg/m3	549.98	Calculated Property
ρl	355.18	kg/m3	588.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[244.60; 570.07]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-4.01200e-02
Coefficient B			-1.86060e+01
Coefficient C			-1.92270e+00
Coefficient D			-1.74870e-03
Coefficient E			-7.27810e-07
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			244.60
Temperature range, max.			570.07
γ	0.04	N/m	244.60	Calculated Property
γ	0.04	N/m	280.76	Calculated Property
γ	0.03	N/m	316.93	Calculated Property
γ	0.03	N/m	353.09	Calculated Property
γ	0.02	N/m	389.25	Calculated Property
γ	0.02	N/m	425.42	Calculated Property
γ	0.01	N/m	461.58	Calculated Property
γ	0.01	N/m	497.74	Calculated Property
γ	0.00	N/m	533.91	Calculated Property
γ	0.00	N/m	570.07	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[244.60; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			3.13930e-05
Coefficient B			1.11170e+00
Coefficient C			-9.19030e+01
Coefficient D			1.28140e+05
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			244.60
Temperature range, max.			1000.00
λgas	0.01	W/m×K	244.60	Calculated Property
λgas	0.01	W/m×K	328.53	Calculated Property
λgas	0.02	W/m×K	412.47	Calculated Property
λgas	0.02	W/m×K	496.40	Calculated Property
λgas	0.03	W/m×K	580.33	Calculated Property
λgas	0.04	W/m×K	664.27	Calculated Property
λgas	0.04	W/m×K	748.20	Calculated Property
λgas	0.05	W/m×K	832.13	Calculated Property
λgas	0.06	W/m×K	916.07	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.23; 0.18]	W/m×K	[244.60; 374.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			5.08890e-02
Coefficient B			-1.50550e+02
Coefficient C			-2.95200e-01
Coefficient D			-2.84030e-03
Coefficient E			-2.21090e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			244.60
Temperature range, max.			374.35
λliquid	0.23	W/m×K	244.60	Calculated Property
λliquid	0.22	W/m×K	259.02	Calculated Property
λliquid	0.22	W/m×K	273.43	Calculated Property
λliquid	0.21	W/m×K	287.85	Calculated Property
λliquid	0.21	W/m×K	302.27	Calculated Property
λliquid	0.20	W/m×K	316.68	Calculated Property
λliquid	0.20	W/m×K	331.10	Calculated Property
λliquid	0.19	W/m×K	345.52	Calculated Property
λliquid	0.18	W/m×K	359.93	Calculated Property
λliquid	0.18	W/m×K	374.35	Calculated Property

Similar Compounds

Find more compounds similar to Methane, nitro-.

Mixtures

• TETRABUTYLAMMONIUM HEXAFLUOROPHOSPHATE + Methane, nitro-
• Ethanol, 2-methoxy- + Methane, nitro-
• Ethanol, 2-butoxy- + Methane, nitro-
• Methane, nitro- + 3-Pentanol
• 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-
• Pentane, 1-chloro- + Methane, nitro-
• Benzene, nitro- + Methane, nitro-
• n-Butyl ether + Methane, nitro-
• Hexane, 1-ethoxy- + Methane, nitro-
• Pentane, 1-propoxy- + Methane, nitro-
• Methane, nitro- + Water
• Acetic acid, pentyl ester + Methane, nitro-
• Carbon dioxide + Methane, nitro-
• Methane, nitro- + Tetrabutylammonium tetrafluoroborate

Find more mixtures with Methane, nitro-.

Sources

• KDB Vapor Pressure Data
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• 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
• Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
• 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
• Thermodynamic and physicochemical properties of binary mixtures of nitromethane with {2-methoxyethanol + 2-butoxyethanol} systems at T = (293.15, 298.15, 303.15, 308.15, and 313.15) 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
• Water as a solute in aprotic dipolar solvents. 2. D2O-H2O solute isotope effects on the enthalpy of water dissolution in nitromethane, acetonitrile and propylene carbonate at 298.15 K
• Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Relative Permittivity and Apparent Dipole Moments of Nitromethane, Nitroethane, 1-Nitropropane and 2- Nitropropane in Several Nonpolar Solvents.
• 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
• Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
• Isobaric Thermal Expansivity of Highly Polar Nitrogen Compounds at Temperatures from (278.15 to 348.15) K and at Pressures from (5 to 55) MPa
• 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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