Chemical Properties of Nitric oxide (CAS 10102-43-9)

InChI

InChI=1S/NO/c1-2

InChI Key

MWUXSHHQAYIFBG-UHFFFAOYSA-N

Formula

NO

SMILES

[N]=O

Molecular Weight¹

30.01

CAS

10102-43-9

Other Names

• Amidogen, oxo-
• NO
• Nitrogen oxide
• UN 1660
• nitrogen monooxide
• nitrogen monoxide
• nitrogen oxide (NO)
• nitrosyl radical
• oxoamidogen

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (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_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : 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	[0.5820; 0.5880]
ω	0.5820		ChemSep v8.3 pure component data
ω	0.5880		KDB
PAff	[526.10; 531.80]	kJ/mol
PAff	531.80	kJ/mol	NIST
PAff	526.10 ± 1.30	kJ/mol	NIST
BasG	505.30	kJ/mol	NIST
μ	[0.15; 0.20]	debye
μ	0.15	debye	ChemSep v8.3 pure component data
μ	0.20	debye	KDB
ΔfG°	[86.57; 86.75]	kJ/mol
ΔfG°	86.57	kJ/mol	ChemSep v8.3 pure component data
ΔfG°	86.75	kJ/mol	KDB
ΔfH°gas	[90.25; 90.43]	kJ/mol
ΔfH°gas	90.25	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	90.43	kJ/mol	KDB
IE	[9.20; 9.54]	eV
IE	9.26 ± 0.00	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.26	eV	NIST
IE	9.26	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.23	eV	NIST
IE	9.20 ± 0.10	eV	NIST
IE	Outlier 9.54	eV	NIST
IE	9.26	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.27	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.27	eV	NIST
IE	9.25 ± 0.02	eV	NIST
IE	9.25 ± 0.15	eV	NIST
IE	9.27	eV	NIST
IE	9.26 ± 0.00	eV	NIST
IE	9.27 ± 0.05	eV	NIST
IE	9.28 ± 0.03	eV	NIST
IE	9.27 ± 0.01	eV	NIST
IE	9.25 ± 0.01	eV	NIST
IE	9.27 ± 0.01	eV	NIST
IE	9.25 ± 0.02	eV	NIST
IE	9.26	eV	NIST
logPoct/wat	-0.447		Crippen Calculated Property
McVol	20.260	ml/mol	McGowan Calculated Property
Pc	[6480.00; 6480.00]	kPa
Pc	6480.00	kPa	ChemSep v8.3 pure component data
Pc	6480.00	kPa	Air Liquide Gas Encyclopedia
Pc	6480.00	kPa	KDB
Ptriple	[21.89; 21.92]	kPa
Ptriple	21.89	kPa	ChemSep v8.3 pure component data
Ptriple	21.89	kPa	Air Liquide Gas Encyclopedia
Ptriple	21.92	kPa	KDB
ρc	517.35	kg/m3	Air Liquide Gas Encyclopedia
Tboil	[121.38; 121.41]	K
Tboil	121.38	K	ChemSep v8.3 pure component data
Tboil	121.38	K	Air Liquide Gas Encyclopedia
Tboil	121.41	K	KDB
Tc	[180.00; 180.15]	K
Tc	180.00	K	ChemSep v8.3 pure component data
Tc	180.15	K	Air Liquide Gas Encyclopedia
Tc	180.00	K	KDB
Tfus	[109.50; 112.15]	K
Tfus	112.15	K	ChemSep v8.3 pure component data
Tfus	112.15	K	Air Liquide Gas Encyclopedia
Tfus	109.50	K	KDB
Ttriple	[109.50; 109.54]	K
Ttriple	109.50	K	ChemSep v8.3 pure component data
Ttriple	109.50	K	Air Liquide Gas Encyclopedia
Ttriple	109.54	K	KDB
UQi	0.99		ChemSep v8.3 pure component data
URi	0.92		ChemSep v8.3 pure component data
Vc	[0.058; 0.058]	m3/kmol
Vc	0.058	m3/kmol	ChemSep v8.3 pure component data
Vc	0.058	m3/kmol	KDB
Zc	[0.2510000; 0.2511270]
Zc	0.2510000		ChemSep v8.3 pure component data
Zc	0.2511270		KDB
Zra	0.27		KDB

Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	2.31	kJ/mol	112.15	Air Liquide Gas Encyclopedia
ΔvapH	[13.53; 13.80]	kJ/mol	[121.38; 212.00]
ΔvapH	13.53	kJ/mol	121.38	Air Liquide Gas Encyclopedia
ΔvapH	13.80	kJ/mol	212.00	NIST
Pvap	[188.30; 987.80]	kPa	[127.32; 146.22]
Pvap	188.30	kPa	127.32	Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air
Pvap	410.90	kPa	135.80	Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air
Pvap	987.80	kPa	146.22	Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air
ρg	3.03	kg/m3	121.38	Air Liquide Gas Encyclopedia
ρl	[1280.00; 1280.84]	kg/m3	[121.00; 121.38]
ρl	1280.00	kg/m3	121.00	KDB
ρl	1280.84	kg/m3	121.38	Air Liquide Gas Encyclopedia

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[29.83; 35.77]	J/mol×K	[50.00; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.98319e+01
Coefficient B			-2.62296e+03
Coefficient C			6.03657e+00
Coefficient D			-2.60975e-03
Coefficient E			6.26147e-07
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			50.00
Temperature range, max.			1500.00
Cp,gas	29.83	J/mol×K	50.00	Calculated Property
Cp,gas	29.83	J/mol×K	211.11	Calculated Property
Cp,gas	29.98	J/mol×K	372.22	Calculated Property
Cp,gas	30.74	J/mol×K	533.33	Calculated Property
Cp,gas	31.95	J/mol×K	694.44	Calculated Property
Cp,gas	33.14	J/mol×K	855.56	Calculated Property
Cp,gas	34.10	J/mol×K	1016.67	Calculated Property
Cp,gas	34.81	J/mol×K	1177.78	Calculated Property
Cp,gas	35.34	J/mol×K	1338.89	Calculated Property
Cp,gas	35.77	J/mol×K	1500.00	Calculated Property
Cp,gas	[29.86; 34.86]	J/mol×K	[298.00; 1200.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.38349e+01
Coefficient B			1.25888e+01
Coefficient C			-1.13901e+00
Coefficient D			-1.49746e+00
Coefficient E			2.14194e-01
Reference			Chase, 1998
Comment			F=83.35783, G=237.1219, H=90.29114; Data last reviewed in June, 1963
Temperature range, min.			298.00
Temperature range, max.			1200.00
Cp,gas	29.86	J/mol×K	298.00	Calculated Property
Cp,gas	29.92	J/mol×K	398.22	Calculated Property
Cp,gas	30.50	J/mol×K	498.44	Calculated Property
Cp,gas	31.24	J/mol×K	598.67	Calculated Property
Cp,gas	32.00	J/mol×K	698.89	Calculated Property
Cp,gas	32.74	J/mol×K	799.11	Calculated Property
Cp,gas	33.41	J/mol×K	899.33	Calculated Property
Cp,gas	34.00	J/mol×K	999.56	Calculated Property
Cp,gas	34.49	J/mol×K	1099.78	Calculated Property
Cp,gas	34.86	J/mol×K	1200.00	Calculated Property
Cp,gas	[34.86; 38.48]	J/mol×K	[1200.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.59917e+01
Coefficient B			9.57170e-01
Coefficient C			-1.48032e-01
Coefficient D			9.97400e-03
Coefficient E			-3.00409e+00
Reference			Chase, 1998
Comment			F=73.10787, G=246.1619, H=90.29114; Data last reviewed in June, 1963
Temperature range, min.			1200.00
Temperature range, max.			6000.00
Cp,gas	34.86	J/mol×K	1200.00	Calculated Property
Cp,gas	36.26	J/mol×K	1733.33	Calculated Property
Cp,gas	36.93	J/mol×K	2266.67	Calculated Property
Cp,gas	37.35	J/mol×K	2800.00	Calculated Property
Cp,gas	37.64	J/mol×K	3333.33	Calculated Property
Cp,gas	37.86	J/mol×K	3866.67	Calculated Property
Cp,gas	38.03	J/mol×K	4400.00	Calculated Property
Cp,gas	38.19	J/mol×K	4933.33	Calculated Property
Cp,gas	38.33	J/mol×K	5466.67	Calculated Property
Cp,gas	38.48	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[63.60; 199.29]	J/mol×K	[109.50; 150.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			3.87560e+01
Coefficient B			-3.23940e+02
Coefficient C			8.77724e+00
Coefficient D			-6.04120e-02
Coefficient E			3.34340e-04
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			109.50
Temperature range, max.			150.00
Cp,liquid	63.60	J/mol×K	109.50	Calculated Property
Cp,liquid	68.53	J/mol×K	114.00	Calculated Property
Cp,liquid	74.62	J/mol×K	118.50	Calculated Property
Cp,liquid	82.19	J/mol×K	123.00	Calculated Property
Cp,liquid	91.69	J/mol×K	127.50	Calculated Property
Cp,liquid	103.75	J/mol×K	132.00	Calculated Property
Cp,liquid	119.18	J/mol×K	136.50	Calculated Property
Cp,liquid	139.11	J/mol×K	141.00	Calculated Property
Cp,liquid	165.09	J/mol×K	145.50	Calculated Property
Cp,liquid	199.29	J/mol×K	150.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0003919; 0.0000384]	Pa×s	[109.15; 180.05]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-5.00980e+01
Coefficient B			7.34630e+02
Coefficient C			8.02670e+00
Coefficient D			-1.79960e-04
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			109.15
Temperature range, max.			180.05
η	0.0003919	Pa×s	109.15	Calculated Property
η	0.0003163	Pa×s	117.03	Calculated Property
η	0.0002549	Pa×s	124.91	Calculated Property
η	0.0002039	Pa×s	132.78	Calculated Property
η	0.0001612	Pa×s	140.66	Calculated Property
η	0.0001256	Pa×s	148.54	Calculated Property
η	0.0000962	Pa×s	156.42	Calculated Property
η	0.0000723	Pa×s	164.29	Calculated Property
η	0.0000533	Pa×s	172.17	Calculated Property
η	0.0000384	Pa×s	180.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[14.49; 4.36]	kJ/mol	[109.50; 176.43]	ChemSep v8.3 pure component data
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			2.47210e+01
Coefficient B			2.23650e+00
Coefficient C			-5.86720e+00
Coefficient D			6.81690e+00
Coefficient E			-2.75290e+00
Critical temperature, Tc (K)			1.80000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			109.50
Temperature range, max.			176.43
ΔvapH	14.49	kJ/mol	109.50	Calculated Property
ΔvapH	13.93	kJ/mol	116.94	Calculated Property
ΔvapH	13.28	kJ/mol	124.37	Calculated Property
ΔvapH	12.55	kJ/mol	131.81	Calculated Property
ΔvapH	11.71	kJ/mol	139.25	Calculated Property
ΔvapH	10.77	kJ/mol	146.68	Calculated Property
ΔvapH	9.70	kJ/mol	154.12	Calculated Property
ΔvapH	8.44	kJ/mol	161.56	Calculated Property
ΔvapH	6.86	kJ/mol	168.99	Calculated Property
ΔvapH	4.36	kJ/mol	176.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[21.96; 6493.35]	kPa	[109.50; 180.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57218e+01
Coefficient B			-1.08919e+03
Coefficient C			-2.32800e+01
Temperature range, min.			109.50
Temperature range, max.			180.15
Pvap	21.96	kPa	109.50	Calculated Property
Pvap	63.01	kPa	117.35	Calculated Property
Pvap	153.71	kPa	125.20	Calculated Property
Pvap	330.08	kPa	133.05	Calculated Property
Pvap	640.05	kPa	140.90	Calculated Property
Pvap	1142.43	kPa	148.75	Calculated Property
Pvap	1904.65	kPa	156.60	Calculated Property
Pvap	2999.94	kPa	164.45	Calculated Property
Pvap	4504.26	kPa	172.30	Calculated Property
Pvap	6493.35	kPa	180.15	Calculated Property
Pvap	[13.23; 6463.65]	kPa	[106.16; 180.15]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			9.17675e+01
Coefficient B			-3.01148e+03
Coefficient C			-1.32112e+01
Coefficient D			7.20780e-05
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			106.16
Temperature range, max.			180.15
Pvap	13.23	kPa	106.16	Calculated Property
Pvap	43.25	kPa	114.38	Calculated Property
Pvap	116.27	kPa	122.60	Calculated Property
Pvap	268.33	kPa	130.82	Calculated Property
Pvap	548.95	kPa	139.04	Calculated Property
Pvap	1020.29	kPa	147.27	Calculated Property
Pvap	1756.02	kPa	155.49	Calculated Property
Pvap	2840.95	kPa	163.71	Calculated Property
Pvap	4372.42	kPa	171.93	Calculated Property
Pvap	6463.65	kPa	180.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1328.56; 465.53]	kg/m3	[109.50; 180.15]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.40750e+01
Coefficient B			1.96860e-01
Coefficient C			1.80160e+02
Coefficient D			1.54430e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			109.50
Temperature range, max.			180.15
ρl	1328.56	kg/m3	109.50	Calculated Property
ρl	1295.31	kg/m3	117.35	Calculated Property
ρl	1259.31	kg/m3	125.20	Calculated Property
ρl	1219.86	kg/m3	133.05	Calculated Property
ρl	1175.94	kg/m3	140.90	Calculated Property
ρl	1125.88	kg/m3	148.75	Calculated Property
ρl	1066.80	kg/m3	156.60	Calculated Property
ρl	992.67	kg/m3	164.45	Calculated Property
ρl	886.52	kg/m3	172.30	Calculated Property
ρl	465.53	kg/m3	180.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 1.88e-04]	N/m	[109.50; 176.43]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-2.84360e-03
Coefficient B			5.51060e+02
Coefficient C			-1.70170e+01
Coefficient D			1.30020e-01
Coefficient E			-4.76890e-04
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			109.50
Temperature range, max.			176.43
γ	0.03	N/m	109.50	Calculated Property
γ	0.02	N/m	116.94	Calculated Property
γ	0.02	N/m	124.37	Calculated Property
γ	0.02	N/m	131.81	Calculated Property
γ	0.01	N/m	139.25	Calculated Property
γ	0.01	N/m	146.68	Calculated Property
γ	0.01	N/m	154.12	Calculated Property
γ	0.00	N/m	161.56	Calculated Property
γ	0.00	N/m	168.99	Calculated Property
γ	1.88e-04	N/m	176.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.06]	W/m×K	[100.00; 750.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			4.66570e-04
Coefficient B			7.33530e-01
Coefficient C			5.89170e+01
Coefficient D			-6.25750e+02
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			100.00
Temperature range, max.			750.00
λ	0.01	W/m×K	100.00	Calculated Property
λ	0.02	W/m×K	172.22	Calculated Property
λ	0.02	W/m×K	244.44	Calculated Property
λ	0.03	W/m×K	316.67	Calculated Property
λ	0.03	W/m×K	388.89	Calculated Property
λ	0.04	W/m×K	461.11	Calculated Property
λ	0.04	W/m×K	533.33	Calculated Property
λ	0.05	W/m×K	605.56	Calculated Property
λ	0.05	W/m×K	677.78	Calculated Property
λ	0.06	W/m×K	750.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.23; 0.08]	W/m×K	[81.00; 176.40]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-8.53840e-01
Coefficient B			4.78680e+00
Coefficient C			-1.00490e-02
Coefficient D			1.04540e-03
Coefficient E			-8.60440e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			81.00
Temperature range, max.			176.40
λ	0.23	W/m×K	81.00	Calculated Property
λ	0.21	W/m×K	91.60	Calculated Property
λ	0.20	W/m×K	102.20	Calculated Property
λ	0.19	W/m×K	112.80	Calculated Property
λ	0.17	W/m×K	123.40	Calculated Property
λ	0.16	W/m×K	134.00	Calculated Property
λ	0.14	W/m×K	144.60	Calculated Property
λ	0.12	W/m×K	155.20	Calculated Property
λ	0.10	W/m×K	165.80	Calculated Property
λ	0.08	W/m×K	176.40	Calculated Property

Similar Compounds

Find more compounds similar to Nitric oxide.

Mixtures

• Carbon dioxide + Nitric oxide
• Nitric oxide + Sulfur dioxide
• Nitric oxide + Argon
• Carbon monoxide + Nitric oxide
• Nitrogen + Nitric oxide
• Nitric oxide + 1H-Tetrazole + Tetrabutylphosphonium bromide
• Tetra-N-butylammonium chloride + Nitric oxide + 1H-Tetrazole
• Nitric oxide + Tetra-N-butylammonium bromide + 1H-Tetrazole
• Choline chloride + Nitric oxide + 1H-Tetrazole
• Choline chloride + Nitric oxide + 1H-1,2,4-Triazole
• Choline chloride + Nitric oxide + 1H-Imidazole
• Nitric oxide + Butane, decafluoro-

Sources

• Air Liquide Gas Encyclopedia
• 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
• Crippen Method
• Thermodynamic Study of binary an ternary systems containing CO2 + impurities in the context of CO2 transportation
• Thermodynamic study of binary systems containing sulphur dioxide and nitric oxide: Measurements and modelling
• Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air
• Efficient and Reversible Nitric Oxide Absorption by Low-Viscosity, Azole-Derived Deep Eutectic Solvents
• Vapor Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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