Chemical Properties of Nitrous oxide (CAS 10024-97-2)

InChI

InChI=1S/N2O/c1-2-3

InChI Key

GQPLMRYTRLFLPF-UHFFFAOYSA-N

Formula

N2O

SMILES

[N-]=[N+]=O

Molecular Weight¹

44.01

CAS

10024-97-2

Other Names

• Dinitrogen monoxide
• Factitious air
• Hyponitrous acid anhydride
• Laughing gas
• N2O
• Nitral
• Nitrogen monoxide
• Nitrogen oxide
• Nitrogen oxide (N2O)
• UN 1070
• UN 2201
• dinitrogen oxide

• 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).
• EA : Electron affinity (eV).
• 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_subH : Enthalpy of sublimation 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).
• I_np : Non-polar retention indices.
• 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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.1620; 0.1733]
ω	0.1733		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1620		ChemSep v8.3 pure component data Compiled value
ω	0.1650		KDB
PAff	[549.80; 575.20]	kJ/mol
PAff	549.80	kJ/mol	NIST
PAff	575.20	kJ/mol	NIST
BasG	[523.30; 548.70]	kJ/mol
BasG	523.30	kJ/mol	NIST
BasG	548.70	kJ/mol	NIST
μ	[0.17; 0.20]	debye
μ	0.17	debye	ChemSep v8.3 pure component data Compiled value
μ	0.20	debye	KDB
EA	[-0.15; 0.76]	eV
EA	0.22 ± 0.10	eV	NIST
EA	-0.15 ± 0.10	eV	NIST
EA	0.27 ± 0.17	eV	NIST
EA	0.76 ± 0.10	eV	NIST
ΔfG°	[103.70; 104.16]	kJ/mol
ΔfG°	104.16	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	103.70	kJ/mol	KDB
ΔfH°gas	[81.60; 82.57]	kJ/mol
ΔfH°gas	82.57 ± 0.10	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	82.05	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	81.60	kJ/mol	KDB
IE	[12.00; 12.91]	eV
IE	12.89 ± 0.00	eV	NIST
IE	12.89	eV	NIST
IE	Outlier 12.00 ± 1.00	eV	NIST
IE	12.91 ± 0.03	eV	NIST
IE	12.89 ± 0.00	eV	NIST
IE	12.88 ± 0.01	eV	NIST
IE	12.89 ± 0.01	eV	NIST
IE	12.90	eV	NIST
IE	12.89 ± 0.01	eV	NIST
IE	12.89 ± 0.01	eV	NIST
IE	12.89	eV	NIST
IE	12.89 ± 0.01	eV	NIST
IE	12.80 ± 0.05	eV	NIST
IE	12.88 ± 0.01	eV	NIST
IE	12.89	eV	NIST
IE	12.89	eV	NIST
logPoct/wat	-0.158		Crippen Calculated Property
McVol	28.090	ml/mol	McGowan Calculated Property
Pc	[7234.60; 7270.00]	kPa
Pc	7244.74	kPa	Mathews (1972), critical constants of inorganic substances Compiled value
Pc	7244.74	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	7255.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	7245.00	kPa	Air Liquide Gas Encyclopedia
Pc	7255.00	kPa	KDB
Pc	7238.00 ± 20.00	kPa	NIST
Pc	Outlier 7270.00 ± 50.00	kPa	NIST
Pc	7234.60 ± 50.66	kPa	NIST
Ptriple	[87.85; 87.91]	kPa
Ptriple	87.86 ± 0.01	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
Ptriple	87.85	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	87.85	kPa	Air Liquide Gas Encyclopedia
Ptriple	87.85	kPa	KDB
Ptriple	87.89 ± 0.01	kPa	NIST
Ptriple	87.91 ± 0.01	kPa	NIST
ρc	[448.93; 453.33]	kg/m3
ρc	452.01	kg/m3	Air Liquide Gas Encyclopedia
ρc	453.33 ± 4.40	kg/m3	NIST
ρc	448.93	kg/m3	NIST
ρc	453.33 ± 2.20	kg/m3	NIST
Inp	[182.00; 182.00]
Inp	182.00		NIST
Inp	182.00		NIST
Tboil	[184.67; 184.68]	K
Tboil	184.67	K	ChemSep v8.3 pure component data Compiled value
Tboil	184.68	K	Air Liquide Gas Encyclopedia
Tboil	184.67	K	KDB
Tc	[309.49; 309.65]	K
Tc	309.56	K	Mathews (1972), critical constants of inorganic substances Compiled value
Tc	309.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	309.60	K	ChemSep v8.3 pure component data Compiled value
Tc	309.52	K	Air Liquide Gas Encyclopedia
Tc	309.57	K	KDB
Tc	309.56 ± 0.15	K	NIST
Tc	309.65 ± 0.20	K	NIST
Tc	309.49	K	NIST
Tc	309.55 ± 0.50	K	NIST
Tfus	[182.30; 182.34]	K
Tfus	182.34	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	182.33	K	ChemSep v8.3 pure component data Compiled value
Tfus	182.33	K	Air Liquide Gas Encyclopedia
Tfus	182.30	K	KDB
Ttriple	[181.99; 182.34]	K
Ttriple	181.99	K	Solid Liquid Equilibria for the CO2 + R23 and N2O + R23 Systems
Ttriple	182.34	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	182.30	K	ChemSep v8.3 pure component data Compiled value
Ttriple	182.33	K	Air Liquide Gas Encyclopedia
Ttriple	182.32	K	KDB
UQi	1.24		ChemSep v8.3 pure component data Compiled value
URi	1.24		ChemSep v8.3 pure component data Compiled value
Vc	[0.096; 0.097]	m3/kmol
Vc	0.097	m3/kmol	Mathews (1972), critical constants of inorganic substances Compiled value
Vc	0.097	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.097	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.097	m3/kmol	KDB
Vc	0.096 ± 0.002	m3/kmol	NIST
VCOSTALD	0.10	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.17		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2730000; 0.2740000]
Zc	0.2740000		Mathews (1972), critical constants of inorganic substances Compiled value
Zc	0.2730000		ChemSep v8.3 pure component data Compiled value
Zc	0.2734100		KDB
Zra	[0.28; 0.28]
Zra	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.28		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	[6.50; 6.54]	kJ/mol	[182.33; 182.40]
ΔfusH	6.54	kJ/mol	182.33	Air Liquide Gas Encyclopedia
ΔfusH	6.50	kJ/mol	182.40	NIST
ΔsubH	[23.60; 25.10]	kJ/mol	[74.00; 165.00]
ΔsubH	25.10 ± 0.40	kJ/mol	74.00	NIST
ΔsubH	23.60	kJ/mol	113.00	NIST
ΔsubH	24.60	kJ/mol	165.00	NIST
ΔvapH	[16.10; 16.50]	kJ/mol	[184.68; 209.00]
ΔvapH	16.47	kJ/mol	184.68	Air Liquide Gas Encyclopedia
ΔvapH	16.50	kJ/mol	184.70	NIST
ΔvapH	16.10	kJ/mol	209.00	NIST
Pvap	[554.70; 3119.90]	kPa	[219.24; 273.08]
Pvap	554.70	kPa	219.24	PVT Properties of Dinitrogen Monoxide
Pvap	626.30	kPa	222.28	PVT Properties of Dinitrogen Monoxide
Pvap	652.80	kPa	223.31	PVT Properties of Dinitrogen Monoxide
Pvap	759.60	kPa	227.32	PVT Properties of Dinitrogen Monoxide
Pvap	760.60	kPa	227.36	PVT Properties of Dinitrogen Monoxide
Pvap	912.10	kPa	232.37	PVT Properties of Dinitrogen Monoxide
Pvap	915.40	kPa	232.43	PVT Properties of Dinitrogen Monoxide
Pvap	1092.90	kPa	237.49	PVT Properties of Dinitrogen Monoxide
Pvap	1294.70	kPa	242.57	PVT Properties of Dinitrogen Monoxide
Pvap	1521.90	kPa	247.65	PVT Properties of Dinitrogen Monoxide
Pvap	1777.00	kPa	252.73	PVT Properties of Dinitrogen Monoxide
Pvap	2061.80	kPa	257.80	PVT Properties of Dinitrogen Monoxide
Pvap	2065.40	kPa	257.87	PVT Properties of Dinitrogen Monoxide
Pvap	2379.00	kPa	262.90	PVT Properties of Dinitrogen Monoxide
Pvap	2381.80	kPa	262.95	PVT Properties of Dinitrogen Monoxide
Pvap	2730.60	kPa	267.98	PVT Properties of Dinitrogen Monoxide
Pvap	2734.00	kPa	268.03	PVT Properties of Dinitrogen Monoxide
Pvap	3119.90	kPa	273.08	PVT Properties of Dinitrogen Monoxide
ρg	[1.87; 2.98]	kg/m3	[184.68; 288.15]
ρg	2.98	kg/m3	184.68	Air Liquide Gas Encyclopedia
ρg	1.87	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[1226.00; 1230.46]	kg/m3	[184.00; 184.68]
ρl	1226.00	kg/m3	184.00	KDB
ρl	1230.46	kg/m3	184.68	Air Liquide Gas Encyclopedia

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[29.32; 58.27]	J/mol×K	[100.00; 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			2.86500e+01
Coefficient B			-4.00030e+02
Coefficient C			3.59224e+00
Coefficient D			1.42920e-04
Coefficient E			-6.72800e-08
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	29.32	J/mol×K	100.00	Calculated Property
Cp,gas	36.49	J/mol×K	255.56	Calculated Property
Cp,gas	43.04	J/mol×K	411.11	Calculated Property
Cp,gas	47.67	J/mol×K	566.67	Calculated Property
Cp,gas	50.99	J/mol×K	722.22	Calculated Property
Cp,gas	53.43	J/mol×K	877.78	Calculated Property
Cp,gas	55.25	J/mol×K	1033.33	Calculated Property
Cp,gas	56.60	J/mol×K	1188.89	Calculated Property
Cp,gas	57.59	J/mol×K	1344.44	Calculated Property
Cp,gas	58.27	J/mol×K	1500.00	Calculated Property
Cp,gas	[38.60; 57.94]	J/mol×K	[298.00; 1400.00]	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			2.76799e+01
Coefficient B			5.11490e+01
Coefficient C			-3.06445e+01
Coefficient D			6.84791e+00
Coefficient E			-1.57906e-01
Reference			Chase, 1998
Comment			F=71.24934, G=238.6164, H=82.04824; Data last reviewed in December, 1964
Temperature range, min.			298.00
Temperature range, max.			1400.00
Cp,gas	38.60	J/mol×K	298.00	Calculated Property
Cp,gas	43.38	J/mol×K	420.44	Calculated Property
Cp,gas	46.98	J/mol×K	542.89	Calculated Property
Cp,gas	49.81	J/mol×K	665.33	Calculated Property
Cp,gas	52.05	J/mol×K	787.78	Calculated Property
Cp,gas	53.82	J/mol×K	910.22	Calculated Property
Cp,gas	55.21	J/mol×K	1032.67	Calculated Property
Cp,gas	56.31	J/mol×K	1155.11	Calculated Property
Cp,gas	57.19	J/mol×K	1277.56	Calculated Property
Cp,gas	57.94	J/mol×K	1400.00	Calculated Property
Cp,gas	[57.91; 62.08]	J/mol×K	[1400.00; 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			6.03027e+01
Coefficient B			1.03457e+00
Coefficient C			-1.92997e-01
Coefficient D			1.25400e-02
Coefficient E			-6.86025e+00
Reference			Chase, 1998
Comment			F=48.61390, G=272.5002, H=82.04824; Data last reviewed in December, 1964
Temperature range, min.			1400.00
Temperature range, max.			6000.00
Cp,gas	57.91	J/mol×K	1400.00	Calculated Property
Cp,gas	59.78	J/mol×K	1911.11	Calculated Property
Cp,gas	60.69	J/mol×K	2422.22	Calculated Property
Cp,gas	61.20	J/mol×K	2933.33	Calculated Property
Cp,gas	61.51	J/mol×K	3444.44	Calculated Property
Cp,gas	61.71	J/mol×K	3955.56	Calculated Property
Cp,gas	61.85	J/mol×K	4466.67	Calculated Property
Cp,gas	61.94	J/mol×K	4977.78	Calculated Property
Cp,gas	62.01	J/mol×K	5488.89	Calculated Property
Cp,gas	62.08	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[77.50; 78.44]	J/mol×K	[182.30; 200.00]	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			7.25250e+01
Coefficient B			2.32930e+02
Coefficient C			-4.64116e+00
Coefficient D			3.73290e-02
Coefficient E			-5.53040e-05
Temperature range, min.			182.30
Temperature range, max.			200.00
Cp,liquid	77.50	J/mol×K	182.30	Calculated Property
Cp,liquid	77.60	J/mol×K	184.27	Calculated Property
Cp,liquid	77.70	J/mol×K	186.23	Calculated Property
Cp,liquid	77.80	J/mol×K	188.20	Calculated Property
Cp,liquid	77.90	J/mol×K	190.17	Calculated Property
Cp,liquid	78.01	J/mol×K	192.13	Calculated Property
Cp,liquid	78.11	J/mol×K	194.10	Calculated Property
Cp,liquid	78.22	J/mol×K	196.07	Calculated Property
Cp,liquid	78.33	J/mol×K	198.03	Calculated Property
Cp,liquid	78.44	J/mol×K	200.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0002141; 0.0000760]	Pa×s	[210.00; 283.09]	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			-1.08760e+01
Coefficient B			4.72990e+02
Coefficient C			1.46590e-01
Coefficient D			-1.38150e-05
Coefficient E			2.00000e+00
Temperature range, min.			210.00
Temperature range, max.			283.09
η	0.0002141	Pa×s	210.00	Calculated Property
η	0.0001887	Pa×s	218.12	Calculated Property
η	0.0001670	Pa×s	226.24	Calculated Property
η	0.0001482	Pa×s	234.36	Calculated Property
η	0.0001320	Pa×s	242.48	Calculated Property
η	0.0001178	Pa×s	250.61	Calculated Property
η	0.0001054	Pa×s	258.73	Calculated Property
η	0.0000944	Pa×s	266.85	Calculated Property
η	0.0000846	Pa×s	274.97	Calculated Property
η	0.0000760	Pa×s	283.09	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[17.13; 0.62]	kJ/mol	[182.30; 309.57]	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			2.58556e+01
Coefficient B			9.82629e-01
Coefficient C			-2.29231e+00
Coefficient D			3.36983e+00
Coefficient E			-1.65657e+00
Critical temperature, Tc (K)			3.09600e+02
Temperature range, min.			182.30
Temperature range, max.			309.57
ΔvapH	17.13	kJ/mol	182.30	Calculated Property
ΔvapH	16.25	kJ/mol	196.44	Calculated Property
ΔvapH	15.28	kJ/mol	210.58	Calculated Property
ΔvapH	14.24	kJ/mol	224.72	Calculated Property
ΔvapH	13.13	kJ/mol	238.86	Calculated Property
ΔvapH	11.92	kJ/mol	253.01	Calculated Property
ΔvapH	10.59	kJ/mol	267.15	Calculated Property
ΔvapH	9.04	kJ/mol	281.29	Calculated Property
ΔvapH	6.99	kJ/mol	295.43	Calculated Property
ΔvapH	0.62	kJ/mol	309.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[86.70; 7259.92]	kPa	[182.30; 309.57]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36769e+01
Coefficient B			-1.26781e+03
Coefficient C			-4.47100e+01
Temperature range, min.			182.30
Temperature range, max.			309.57
Pvap	86.70	kPa	182.30	Calculated Property
Pvap	204.63	kPa	196.44	Calculated Property
Pvap	417.19	kPa	210.58	Calculated Property
Pvap	760.49	kPa	224.72	Calculated Property
Pvap	1270.20	kPa	238.86	Calculated Property
Pvap	1978.80	kPa	253.01	Calculated Property
Pvap	2913.74	kPa	267.15	Calculated Property
Pvap	4096.48	kPa	281.29	Calculated Property
Pvap	5542.17	kPa	295.43	Calculated Property
Pvap	7259.92	kPa	309.57	Calculated Property
Pvap	[71.67; 7193.85]	kPa	[179.17; 309.57]	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			4.37889e+01
Coefficient B			-2.83647e+03
Coefficient C			-4.60994e+00
Coefficient D			7.23732e-06
Coefficient E			2.00000e+00
Temperature range, min.			179.17
Temperature range, max.			309.57
Pvap	71.67	kPa	179.17	Calculated Property
Pvap	170.23	kPa	193.66	Calculated Property
Pvap	352.92	kPa	208.15	Calculated Property
Pvap	657.22	kPa	222.64	Calculated Property
Pvap	1123.33	kPa	237.13	Calculated Property
Pvap	1791.31	kPa	251.61	Calculated Property
Pvap	2699.17	kPa	266.10	Calculated Property
Pvap	3881.70	kPa	280.59	Calculated Property
Pvap	5370.38	kPa	295.08	Calculated Property
Pvap	7193.85	kPa	309.57	Calculated Property
Pvap	[0.12; 108.65]	kPa	[129.80; 187.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46859e+01
Coefficient B			-1.43008e+03
Coefficient C			-4.46590e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			129.80
Temperature range, max.			187.70
Pvap	0.12	kPa	129.80	Calculated Property
Pvap	0.39	kPa	136.23	Calculated Property
Pvap	1.10	kPa	142.67	Calculated Property
Pvap	2.70	kPa	149.10	Calculated Property
Pvap	5.98	kPa	155.53	Calculated Property
Pvap	12.12	kPa	161.97	Calculated Property
Pvap	22.85	kPa	168.40	Calculated Property
Pvap	40.45	kPa	174.83	Calculated Property
Pvap	67.85	kPa	181.27	Calculated Property
Pvap	108.65	kPa	187.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1252.81; 459.49]	kg/m3	[182.30; 309.55]	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			9.23301e+01
Coefficient B			2.33800e-01
Coefficient C			3.09600e+02
Coefficient D			2.58990e-01
Temperature range, min.			182.30
Temperature range, max.			309.55
ρl	1252.81	kg/m3	182.30	Calculated Property
ρl	1210.12	kg/m3	196.44	Calculated Property
ρl	1164.94	kg/m3	210.58	Calculated Property
ρl	1116.68	kg/m3	224.72	Calculated Property
ρl	1064.44	kg/m3	238.86	Calculated Property
ρl	1006.83	kg/m3	252.99	Calculated Property
ρl	941.46	kg/m3	267.13	Calculated Property
ρl	863.46	kg/m3	281.27	Calculated Property
ρl	759.53	kg/m3	295.41	Calculated Property
ρl	459.49	kg/m3	309.55	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 1.31e-05]	N/m	[173.15; 307.66]	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			-1.23640e-02
Coefficient B			-1.24210e+02
Coefficient C			-1.42990e+00
Coefficient D			-4.11480e-03
Coefficient E			-1.36530e-05
Comment			Range stopped where the equation turns negative; ChemSep gives it to 309.57 K.
Temperature range, min.			173.15
Temperature range, max.			307.66
γ	0.03	N/m	173.15	Calculated Property
γ	0.02	N/m	188.10	Calculated Property
γ	0.02	N/m	203.04	Calculated Property
γ	0.02	N/m	217.99	Calculated Property
γ	0.01	N/m	232.93	Calculated Property
γ	0.01	N/m	247.88	Calculated Property
γ	0.01	N/m	262.82	Calculated Property
γ	0.00	N/m	277.77	Calculated Property
γ	0.00	N/m	292.71	Calculated Property
γ	1.31e-05	N/m	307.66	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[180.00; 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			1.12100e-03
Coefficient B			6.62980e-01
Coefficient C			5.24680e+02
Coefficient D			7.33270e+03
Temperature range, min.			180.00
Temperature range, max.			1000.00
λgas	0.01	W/m×K	180.00	Calculated Property
λgas	0.02	W/m×K	271.11	Calculated Property
λgas	0.02	W/m×K	362.22	Calculated Property
λgas	0.03	W/m×K	453.33	Calculated Property
λgas	0.04	W/m×K	544.44	Calculated Property
λgas	0.04	W/m×K	635.56	Calculated Property
λgas	0.05	W/m×K	726.67	Calculated Property
λgas	0.06	W/m×K	817.78	Calculated Property
λgas	0.06	W/m×K	908.89	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.10; 0.10]	W/m×K	[277.59; 287.09]	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			1.01120e-01
Coefficient B			-5.27410e+03
Coefficient C			1.67780e+01
Coefficient D			-3.77290e-02
Coefficient E			-4.86780e-05
Temperature range, min.			277.59
Temperature range, max.			287.09
λliquid	0.10	W/m×K	277.59	Calculated Property
λliquid	0.10	W/m×K	278.65	Calculated Property
λliquid	0.10	W/m×K	279.70	Calculated Property
λliquid	0.10	W/m×K	280.76	Calculated Property
λliquid	0.10	W/m×K	281.81	Calculated Property
λliquid	0.10	W/m×K	282.87	Calculated Property
λliquid	0.10	W/m×K	283.92	Calculated Property
λliquid	0.10	W/m×K	284.98	Calculated Property
λliquid	0.10	W/m×K	286.03	Calculated Property
λliquid	0.10	W/m×K	287.09	Calculated Property

Similar Compounds

Find more compounds similar to Nitrous oxide.

Mixtures

• Nitrous oxide + Water
• Ethanol, 2-(ethylamino)- + Nitrous oxide
• Ethanol, 2-(ethylamino)- + Nitrous oxide + Water
• Nitrous oxide + Methane, trifluoro-
• Methane, difluoro- + Nitrous oxide
• Nitrous oxide + Methyl fluoride
• Nitrous oxide + Hydrochloric acid
• Nitrous oxide + Methyl fluoride + Hydrochloric acid
• Nitrous oxide + Ethanol, 2-methoxy-
• Nitrous oxide + Monoethanolamine + Ethanol, 2-methoxy-
• Nitrous oxide + Ethanol, 2-ethoxy-
• Nitrous oxide + Monoethanolamine + Ethanol, 2-ethoxy-
• Nitrous oxide + Monoethanolamine
• Nitrous oxide + Tromethamine + Water
• Nitrous oxide + 1,2-Ethanediol + Water
• Nitrous oxide + 1,2-Ethanediol
• Nitrous oxide + Ethylammonium nitrate
• Nitrous oxide + Nitrogen
• Nitrous oxide + Monoethanolamine + Water
• Nitrous oxide + 1,4-Butanediamine + Water

Find more mixtures with Nitrous oxide.

Sources

• Air Liquide Gas Encyclopedia
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• 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
• Burnett Measurements and Virial Coefficients for the R32+N2O System
• Virial Coefficients from Burnett Measurements for the R23 + N2O System
• Solid Liquid Equilibria for the CO2 + R23 and N2O + R23 Systems
• Phase Behavior of N2O and CO2 in Room-Temperature Ionic Liquids [bmim][Tf2N], [bmim][BF4], [bmim][N(CN)2], [bmim][Ac], [eam][NO3], and [bmim][SCN]
• Binary Diffusion Coefficient Data of Various Gas Systems Determined Using a Loschmidt Cell and Holographic Interferometry
• PVTx measurements for N2O+CH3F, N2O+CH2F2, and N2O+ CHF3 binary systems
• solubility of carbon dioxide in aqueous solutions of 2-aimno-2-hydroxymethyl-1,3-propanediol
• Solubility of carbon dioxide, nitrous oxide and methane in ionic liquids at pressures close to atmospheric
• (Vapour + liquid) equilibria of {xCH3Cl + (1-x)HCl} at temperatures (159.01 and 182.33) K
• Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K
• Vapour pressure and excess Gibbs free energy of the ternary system {x1CH3F + x2HCl + x3N2O} at temperature of 182.33 K
• Automated apparatus for gas solubility measurements
• Solubility of carbon dioxide, nitrous oxide, ethane, and nitrogen in 1-butyl-1-methylpyrrolidinium and trihexyl(tetradecyl)phosphonium tris(pentafluoroethyl)trifluorophosphate (eFAP) ionic liquids
• Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
• Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
• An experimental and modeling study of physical N2O solubility in 2-(ethylamino)ethanol
• Measurement and Correlation of the Physicochemical Properties of Novel Aqueous Bis(3-aminopropyl)amine and Its Blend with N-Methyldiethanolamine for CO2 Capture
• Physicochemical Properties of Aqueous Potassium Salts of Basic Amino Acids as Absorbents for CO2 Capture
• Density, Viscosity and N2O solubility of Aqueous 2- (methylamino)ethanol Solution
• Solubility of Nitrous Oxide in Aqueous Methyldiethanolamine Solutions
• Density, Viscosity, and N2O Solubility of Aqueous Solutions of MEA, BmimBF4, and Their Mixtures from 293.15 to 333.15 K
• Experimental Study of a Hydrophobic Solvent for Natural Gas Sweetening Based on the Solubility and Selectivity for Light Hydrocarbons (CH4, C2H6) and Acid Gases (CO2 and H2S) at 298-353 K
• Physical Solubility and Diffusivity of N2O and CO2 into Aqueous Solutions of (2-Amino-2-methyl-1-propanol + Diethanolamine) and (N-Methyldiethanolamine + Diethanolamine)
• Isochoric PVTx measurements for CO2 + N2O binary system
• PVT Properties of Dinitrogen Monoxide
• Solubility of N2O in and Density, Viscosity, and Surface Tension of Aqueous Piperazine Solutions
• Isochoric PVTx measurements for the C2H6 + N2O binary system
• Physical Solubility and Diffusivity of N2O and CO2 in Aqueous Sodium Glycinate Solutions
• Isochoric PVTx Measurements for the N2O + R125 Binary System
• Solid-Liquid Equilibria for the CO2 + R125 and N2O + R125 Systems: A New Apparatus
• Solubility of N2O in and Density and Viscosity of Aqueous Solutions of Piperazine, Ammonia, and Their Mixtures from (283.15 to 323.15) K
• Solubility of N2O in Density and Viscosity of Aqueous Solutions of 1,4-Butanediamine, 2-(Diethylamino)-ethanol, and Their Mixtures from (298.15 to 333.15) K
• Solid-Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems
• Diffusion Coefficients of N2O in Aqueous Piperazine Solutions Using the Taylor Dispersion Technique from (293 to 333) K and (0.3 to 1.4) mol *dm-3
• Solubility of N2O in Aqueous Solution of Diethylenetriamine
• Physicochemical Properties of Aqueous Solutions of 2-Amino-2-hydroxymethyl-1,3-propanediol
• Physicochemical Properties of Aqueous Solutions of 2-(1-Piperazinyl)-ethylamine
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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