Chemical Properties of Ethane, nitro- (CAS 79-24-3)

InChI

InChI=1S/C2H5NO2/c1-2-3(4)5/h2H2,1H3

InChI Key

MCSAJNNLRCFZED-UHFFFAOYSA-N

Formula

C2H5NO2

SMILES

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

Molecular Weight¹

75.07

CAS

79-24-3

Other Names

• C2H5NO2
• NE
• Nitroetan
• Nitroethane
• Nitroparaffin
• UN 2842

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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).
• 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_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).
• γ : Surface Tension (N/m).
• 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.3410; 0.6723]
ω	0.6723		ChemSep v8.3 pure component data Compiled value
ω	0.3410		KDB
PAff	765.70	kJ/mol	NIST
BasG	733.20	kJ/mol	NIST
ΔcH°liquid	[-1361.60; -1358.00]	kJ/mol
ΔcH°liquid	-1358.00 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-1358.00 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-1361.60 ± 1.30	kJ/mol	NIST
μ	3.66	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-4.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-102.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°liquid	[-144.00; -140.10]	kJ/mol
ΔfH°liquid	-144.00 ± 0.40	kJ/mol	NIST
ΔfH°liquid	-143.60 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-140.10 ± 1.30	kJ/mol	NIST
ΔfusH°	12.30	kJ/mol	Joback Calculated Property
ΔvapH°	41.60 ± 0.42	kJ/mol	NIST
IE	[10.88; 11.02]	eV
IE	10.90 ± 0.05	eV	NIST
IE	10.92 ± 0.01	eV	NIST
IE	10.88 ± 0.05	eV	NIST
IE	11.02	eV	NIST
log10WS	[-0.22; -0.22]
log10WS	-0.22		Aq. Solubility Prediction
log10WS	-0.22		Estimated Solubility
logPoct/wat	0.283		Crippen Calculated Property
McVol	56.460	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
NFPA Safety	2		KDB
Pc	[4850.00; 5160.00]	kPa
Pc	5160.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4850.00	kPa	KDB
Ptriple	3.18e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[567.80; 655.00]
Inp	618.58		NIST
Inp	619.51		NIST
Inp	620.51		NIST
Inp	616.27		NIST
Inp	615.97		NIST
Inp	615.90		NIST
Inp	616.07		NIST
Inp	616.25		NIST
Inp	616.67		NIST
Inp	617.22		NIST
Inp	617.81		NIST
Inp	Outlier 567.80		NIST
Inp	Outlier 572.00		NIST
Inp	638.00		NIST
Inp	638.00		NIST
Inp	634.00		NIST
Inp	592.00		NIST
Inp	609.00		NIST
Inp	623.00		NIST
Inp	598.00		NIST
Inp	590.00		NIST
Inp	583.00		NIST
Inp	636.89		NIST
Inp	590.00		NIST
Inp	618.00		NIST
Inp	623.00		NIST
Inp	618.00		NIST
Inp	Outlier 655.00		NIST
Inp	590.00		NIST
Inp	618.58		NIST
Inp	615.90		NIST
Inp	617.81		NIST
Inp	634.00		NIST
Ip	[1161.00; 1199.20]
Ip	1161.00		NIST
Ip	1194.20		NIST
Ip	1196.20		NIST
Ip	1199.20		NIST
Ip	1179.40		NIST
Ip	1181.30		NIST
Ip	1183.90		NIST
Ip	1187.30		NIST
Ip	1190.20		NIST
Ip	1168.00		NIST
Ip	1161.00		NIST
Tboil	[387.00; 388.20]	K
Tboil	387.22	K	ChemSep v8.3 pure component data Compiled value
Tboil	387.20	K	KDB
Tboil	388.20	K	NIST
Tboil	387.90 ± 0.25	K	NIST
Tboil	387.22 ± 0.05	K	NIST
Tboil	387.40 ± 0.60	K	NIST
Tboil	387.00 ± 0.60	K	NIST
Tboil	387.65 ± 2.00	K	NIST
Tc	[557.15; 595.00]	K
Tc	557.15	K	ChemSep v8.3 pure component data Compiled value
Tc	595.00	K	KDB
Tfus	[183.63; 223.00]	K
Tfus	183.63	K	ChemSep v8.3 pure component data Compiled value
Tfus	223.00	K	KDB
Tfus	183.90	K	Aq. Solubility Prediction
Tfus	183.63 ± 0.05	K	NIST
Ttriple	[183.63; 183.69]	K
Ttriple	183.63	K	ChemSep v8.3 pure component data Compiled value
Ttriple	183.69 ± 0.04	K	NIST
UQi	2.41		ChemSep v8.3 pure component data Compiled value
URi	2.68		ChemSep v8.3 pure component data Compiled value
Vc	0.236	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2470000		ChemSep v8.3 pure component data Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	134.22	J/mol×K	298.15	NIST
ΔfusH	[9.85; 9.85]	kJ/mol	[183.69; 183.70]
ΔfusH	9.85	kJ/mol	183.69	NIST
ΔfusH	9.85	kJ/mol	183.70	NIST
ΔfusH	9.85	kJ/mol	183.70	NIST
ΔvapH	[35.15; 41.30]	kJ/mol	[319.50; 387.20]
ΔvapH	41.30	kJ/mol	319.50	NIST
ΔvapH	38.60	kJ/mol	356.00	NIST
ΔvapH	35.15	kJ/mol	387.20	KDB
Pvap	[6.10; 33.11]	kPa	[313.15; 353.15]
Pvap	6.10	kPa	313.15	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
Pvap	33.11	kPa	353.15	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
n0	[1.38950; 1.38980]		[298.15; 298.15]
n0	1.38951		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	1.38950		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	1.38980		298.15	Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K
ΔfusS	53.64	J/mol×K	183.69	NIST

Datasets

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	0.0011
278.15	10000.00	0.0011
278.15	15000.00	0.0011
278.15	20000.00	0.0011
278.15	25000.00	0.0010
278.15	30000.00	0.0010
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	0.0009
288.15	5000.00	0.0011
288.15	10000.00	0.0011
288.15	15000.00	0.0011
288.15	20000.00	0.0011
288.15	25000.00	0.0010
288.15	30000.00	0.0010
288.15	35000.00	0.0010
288.15	40000.00	0.0010
288.15	45000.00	0.0010
288.15	50000.00	0.0010
288.15	55000.00	0.0009
298.15	5000.00	0.0012
298.15	10000.00	0.0011
298.15	15000.00	0.0011
298.15	20000.00	0.0011
298.15	25000.00	0.0011
298.15	30000.00	0.0010
298.15	35000.00	0.0010
298.15	40000.00	0.0010
298.15	45000.00	0.0010
298.15	50000.00	0.0010
298.15	55000.00	0.0009
308.15	5000.00	0.0012
308.15	10000.00	0.0011
308.15	15000.00	0.0011
308.15	20000.00	0.0011
308.15	25000.00	0.0011
308.15	30000.00	0.0010
308.15	35000.00	0.0010
308.15	40000.00	0.0010
308.15	45000.00	0.0010
308.15	50000.00	0.0010
308.15	55000.00	0.0009
318.15	5000.00	0.0012
318.15	10000.00	0.0012
318.15	15000.00	0.0011
318.15	20000.00	0.0011
318.15	25000.00	0.0011
318.15	30000.00	0.0010
318.15	35000.00	0.0010
318.15	40000.00	0.0010
318.15	45000.00	0.0010
318.15	50000.00	0.0010
318.15	55000.00	0.0009
328.15	5000.00	0.0012
328.15	10000.00	0.0012
328.15	15000.00	0.0011
328.15	20000.00	0.0011
328.15	25000.00	0.0011
328.15	30000.00	0.0010
328.15	35000.00	0.0010
328.15	40000.00	0.0010
328.15	45000.00	0.0010
328.15	50000.00	0.0010
328.15	55000.00	0.0009
338.15	5000.00	0.0012
338.15	10000.00	0.0012
338.15	15000.00	0.0011
338.15	20000.00	0.0011
338.15	25000.00	0.0011
338.15	30000.00	0.0011
338.15	35000.00	0.0010
338.15	40000.00	0.0010
338.15	45000.00	0.0010
338.15	50000.00	0.0010
338.15	55000.00	0.0009
348.15	5000.00	0.0013
348.15	10000.00	0.0012
348.15	15000.00	0.0012
348.15	20000.00	0.0011
348.15	25000.00	0.0011
348.15	30000.00	0.0011
348.15	35000.00	0.0010
348.15	40000.00	0.0010
348.15	45000.00	0.0010
348.15	50000.00	0.0010
348.15	55000.00	0.0009
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[52.68; 192.51]	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			4.81980e+01
Coefficient B			-5.81790e+02
Coefficient C			5.37524e+00
Coefficient D			2.38380e-05
Coefficient E			-2.27390e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	52.68	J/mol×K	150.00	Calculated Property
Cp,gas	79.42	J/mol×K	300.00	Calculated Property
Cp,gas	107.85	J/mol×K	450.00	Calculated Property
Cp,gas	130.61	J/mol×K	600.00	Calculated Property
Cp,gas	148.14	J/mol×K	750.00	Calculated Property
Cp,gas	161.70	J/mol×K	900.00	Calculated Property
Cp,gas	172.30	J/mol×K	1050.00	Calculated Property
Cp,gas	180.66	J/mol×K	1200.00	Calculated Property
Cp,gas	187.28	J/mol×K	1350.00	Calculated Property
Cp,gas	192.51	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[133.93; 157.78]	J/mol×K	[183.63; 387.22]	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			6.79900e+01
Coefficient B			7.98520e+02
Coefficient C			-4.42036e+00
Coefficient D			2.81600e-02
Coefficient E			-2.70010e-05
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			183.63
Temperature range, max.			387.22
Cp,liquid	133.93	J/mol×K	183.63	Calculated Property
Cp,liquid	128.98	J/mol×K	206.25	Calculated Property
Cp,liquid	128.28	J/mol×K	228.87	Calculated Property
Cp,liquid	130.11	J/mol×K	251.49	Calculated Property
Cp,liquid	133.55	J/mol×K	274.11	Calculated Property
Cp,liquid	138.04	J/mol×K	296.74	Calculated Property
Cp,liquid	143.13	J/mol×K	319.36	Calculated Property
Cp,liquid	148.39	J/mol×K	341.98	Calculated Property
Cp,liquid	153.41	J/mol×K	364.60	Calculated Property
Cp,liquid	157.78	J/mol×K	387.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0034182; 0.0002258]	Pa×s	[200.00; 457.00]	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			1.54030e+01
Coefficient B			1.94750e+02
Coefficient C			-4.22170e+00
Coefficient D			7.81260e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			200.00
Temperature range, max.			457.00
η	0.0034182	Pa×s	200.00	Calculated Property
η	0.0018958	Pa×s	228.56	Calculated Property
η	0.0011692	Pa×s	257.11	Calculated Property
η	0.0007843	Pa×s	285.67	Calculated Property
η	0.0005637	Pa×s	314.22	Calculated Property
η	0.0004293	Pa×s	342.78	Calculated Property
η	0.0003438	Pa×s	371.33	Calculated Property
η	0.0002877	Pa×s	399.89	Calculated Property
η	0.0002504	Pa×s	428.44	Calculated Property
η	0.0002258	Pa×s	457.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[47.74; 21.29]	kJ/mol	[183.63; 549.91]	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			5.42869e+01
Coefficient B			3.14015e-01
Coefficient C			-2.25443e-01
Coefficient D			1.06865e+00
Coefficient E			-9.53684e-01
Critical temperature, Tc (K)			5.57150e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			183.63
Temperature range, max.			549.91
ΔvapH	47.74	kJ/mol	183.63	Calculated Property
ΔvapH	45.70	kJ/mol	224.33	Calculated Property
ΔvapH	43.42	kJ/mol	265.03	Calculated Property
ΔvapH	40.94	kJ/mol	305.72	Calculated Property
ΔvapH	38.34	kJ/mol	346.42	Calculated Property
ΔvapH	35.69	kJ/mol	387.12	Calculated Property
ΔvapH	33.08	kJ/mol	427.82	Calculated Property
ΔvapH	30.53	kJ/mol	468.51	Calculated Property
ΔvapH	27.82	kJ/mol	509.21	Calculated Property
ΔvapH	21.29	kJ/mol	549.91	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[285.14; 412.27]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52739e+01
Coefficient B			-3.77809e+03
Coefficient C			-3.30350e+01
Temperature range, min.			285.14
Temperature range, max.			412.27
Pvap	1.33	kPa	285.14	Calculated Property
Pvap	2.95	kPa	299.27	Calculated Property
Pvap	6.04	kPa	313.39	Calculated Property
Pvap	11.52	kPa	327.52	Calculated Property
Pvap	20.73	kPa	341.64	Calculated Property
Pvap	35.42	kPa	355.77	Calculated Property
Pvap	57.87	kPa	369.89	Calculated Property
Pvap	90.89	kPa	384.02	Calculated Property
Pvap	137.84	kPa	398.14	Calculated Property
Pvap	202.65	kPa	412.27	Calculated Property
Pvap	[4.15e-05; 4784.72]	kPa	[183.63; 595.00]	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			7.41261e+01
Coefficient B			-7.18831e+03
Coefficient C			-8.68036e+00
Coefficient D			5.31960e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			183.63
Temperature range, max.			595.00
Pvap	4.15e-05	kPa	183.63	Calculated Property
Pvap	0.02	kPa	229.34	Calculated Property
Pvap	0.70	kPa	275.05	Calculated Property
Pvap	8.77	kPa	320.75	Calculated Property
Pvap	53.36	kPa	366.46	Calculated Property
Pvap	204.67	kPa	412.17	Calculated Property
Pvap	578.86	kPa	457.88	Calculated Property
Pvap	1331.18	kPa	503.58	Calculated Property
Pvap	2653.08	kPa	549.29	Calculated Property
Pvap	4784.72	kPa	595.00	Calculated Property
Pvap	[5.26e-05; 5001.53]	kPa	[183.63; 593.00]	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			6.04445e+01
Coefficient B			-6.61641e+03
Coefficient C			-6.59835e+00
Coefficient D			3.87418e-06
Coefficient E			0.00000e+00
Temperature range, min.			183.63
Temperature range, max.			593.00
Pvap	5.26e-05	kPa	183.63	Calculated Property
Pvap	0.02	kPa	229.12	Calculated Property
Pvap	0.66	kPa	274.60	Calculated Property
Pvap	8.23	kPa	320.09	Calculated Property
Pvap	50.58	kPa	365.57	Calculated Property
Pvap	198.20	kPa	411.06	Calculated Property
Pvap	574.39	kPa	456.54	Calculated Property
Pvap	1351.02	kPa	502.03	Calculated Property
Pvap	2741.27	kPa	547.51	Calculated Property
Pvap	5001.53	kPa	593.00	Calculated Property
Pvap	[106.35; 448.76]	kPa	[390.00; 459.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			8.62712e+00
Coefficient B			-4.78417e+02
Coefficient C			-2.69200e+02
Reference			Tolstova, Kogan, et al., 1965
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			390.00
Temperature range, max.			459.00
Pvap	106.35	kPa	390.00	Calculated Property
Pvap	134.70	kPa	397.67	Calculated Property
Pvap	166.13	kPa	405.33	Calculated Property
Pvap	200.37	kPa	413.00	Calculated Property
Pvap	237.12	kPa	420.67	Calculated Property
Pvap	276.09	kPa	428.33	Calculated Property
Pvap	317.00	kPa	436.00	Calculated Property
Pvap	359.58	kPa	443.67	Calculated Property
Pvap	403.58	kPa	451.33	Calculated Property
Pvap	448.76	kPa	459.00	Calculated Property
Pvap	[0.13; 101.24]	kPa	[252.00; 387.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.54565e+01
Coefficient B			-3.84823e+03
Coefficient C			-3.19630e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			252.00
Temperature range, max.			387.00
Pvap	0.13	kPa	252.00	Calculated Property
Pvap	0.40	kPa	267.00	Calculated Property
Pvap	1.07	kPa	282.00	Calculated Property
Pvap	2.55	kPa	297.00	Calculated Property
Pvap	5.55	kPa	312.00	Calculated Property
Pvap	11.17	kPa	327.00	Calculated Property
Pvap	21.00	kPa	342.00	Calculated Property
Pvap	37.23	kPa	357.00	Calculated Property
Pvap	62.76	kPa	372.00	Calculated Property
Pvap	101.24	kPa	387.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1166.48; 326.81]	kg/m3	[183.63; 593.00]	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			6.75652e+01
Coefficient B			2.24510e-01
Coefficient C			5.93010e+02
Coefficient D			2.63590e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			183.63
Temperature range, max.			593.00
ρl	1166.48	kg/m3	183.63	Calculated Property
ρl	1119.16	kg/m3	229.12	Calculated Property
ρl	1069.46	kg/m3	274.60	Calculated Property
ρl	1016.81	kg/m3	320.09	Calculated Property
ρl	960.35	kg/m3	365.57	Calculated Property
ρl	898.76	kg/m3	411.06	Calculated Property
ρl	829.75	kg/m3	456.54	Calculated Property
ρl	748.70	kg/m3	502.03	Calculated Property
ρl	643.01	kg/m3	547.51	Calculated Property
ρl	326.81	kg/m3	593.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.00]	N/m	[183.63; 549.91]	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			-2.43760e-03
Coefficient B			3.42160e+02
Coefficient C			-7.04020e+00
Coefficient D			1.67270e-02
Coefficient E			-2.78830e-05
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			183.63
Temperature range, max.			549.91
γ	0.05	N/m	183.63	Calculated Property
γ	0.04	N/m	224.33	Calculated Property
γ	0.04	N/m	265.03	Calculated Property
γ	0.03	N/m	305.72	Calculated Property
γ	0.02	N/m	346.42	Calculated Property
γ	0.02	N/m	387.12	Calculated Property
γ	0.01	N/m	427.82	Calculated Property
γ	0.01	N/m	468.51	Calculated Property
γ	0.00	N/m	509.21	Calculated Property
γ	0.00	N/m	549.91	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.07]	W/m×K	[183.63; 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			1.10640e-03
Coefficient B			6.91860e-01
Coefficient C			6.75030e+02
Coefficient D			2.36860e+05
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			183.63
Temperature range, max.			1000.00
λgas	0.00	W/m×K	183.63	Calculated Property
λgas	0.01	W/m×K	274.34	Calculated Property
λgas	0.01	W/m×K	365.05	Calculated Property
λgas	0.02	W/m×K	455.75	Calculated Property
λgas	0.03	W/m×K	546.46	Calculated Property
λgas	0.04	W/m×K	637.17	Calculated Property
λgas	0.04	W/m×K	727.88	Calculated Property
λgas	0.05	W/m×K	818.58	Calculated Property
λgas	0.06	W/m×K	909.29	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.14]	W/m×K	[183.63; 387.22]	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			-1.48600e-01
Coefficient B			6.32400e+00
Coefficient C			-1.07080e+00
Coefficient D			9.66300e-05
Coefficient E			-1.59810e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			183.63
Temperature range, max.			387.22
λliquid	0.19	W/m×K	183.63	Calculated Property
λliquid	0.19	W/m×K	206.25	Calculated Property
λliquid	0.18	W/m×K	228.87	Calculated Property
λliquid	0.18	W/m×K	251.49	Calculated Property
λliquid	0.17	W/m×K	274.11	Calculated Property
λliquid	0.16	W/m×K	296.74	Calculated Property
λliquid	0.16	W/m×K	319.36	Calculated Property
λliquid	0.15	W/m×K	341.98	Calculated Property
λliquid	0.14	W/m×K	364.60	Calculated Property
λliquid	0.14	W/m×K	387.22	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, nitro-.

Mixtures

• Butane, 1,4-dichloro- + Ethane, nitro-
• Butane, 1-chloro- + Ethane, nitro-
• Ethane, nitro- + Pentane, 1-chloro-
• Ethane, nitro- + Ethane, 1,2-dichloro-
• Ethane, nitro- + Propane, 1,3-dichloro-
• Ethane, nitro- + 2-Propanol, 1-methoxy-
• Ethane, nitro- + Cyclohexane
• Ethane, nitro- + Carbon Tetrachloride
• p-Xylene + Ethane, 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
• 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
• Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
• Relative Permittivity and Apparent Dipole Moments of Nitromethane, Nitroethane, 1-Nitropropane and 2- Nitropropane in Several Nonpolar Solvents.
• Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
• Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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