Chemical Properties of Propanenitrile (CAS 107-12-0)

InChI

InChI=1S/C3H5N/c1-2-3-4/h2H2,1H3

InChI Key

FVSKHRXBFJPNKK-UHFFFAOYSA-N

Formula

C3H5N

SMILES

CCC#N

Molecular Weight¹

55.08

CAS

107-12-0

Other Names

• C2H5CN
• CYANOETHANE
• ETHER CYANATUS
• Ethyl cyanide
• Ethylkyanid
• HYDROCYANIC ETHER
• NSC 7966
• PROPIONITRILE
• Propannitril
• Propionic nitrile
• Propiononitrile
• Propylnitrile
• Rcra waste number P101
• UN 2404
• ethanecarbonitrile
• n-Propanenitrile
• propanonitrile

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• 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).
• 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_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3130		KDB
PAff	794.10	kJ/mol	NIST
BasG	763.00	kJ/mol	NIST
ΔcH°liquid	[-1948.30; -1918.00]	kJ/mol
ΔcH°liquid	-1948.30 ± 0.54	kJ/mol	NIST
ΔcH°liquid	-1918.00	kJ/mol	NIST
μ	3.70	debye	KDB
EA	0.02 ± 0.00	eV	NIST
ΔfG°	96.21	kJ/mol	KDB
ΔfH°gas	[50.66; 51.46]	kJ/mol
ΔfH°gas	50.66	kJ/mol	KDB
ΔfH°gas	51.46	kJ/mol	NIST
ΔfH°liquid	15.50	kJ/mol	NIST
ΔfusH°	5.03	kJ/mol	Joback Calculated Property
ΔvapH°	[36.00; 37.10]	kJ/mol
ΔvapH°	36.19	kJ/mol	NIST
ΔvapH°	37.10 ± 0.30	kJ/mol	NIST
ΔvapH°	36.00	kJ/mol	NIST
ΔvapH°	36.00	kJ/mol	NIST
ΔvapH°	36.03 ± 0.02	kJ/mol	NIST
ΔvapH°	36.70 ± 0.30	kJ/mol	NIST
IE	[11.50; 11.90]	eV
IE	11.85 ± 0.02	eV	NIST
IE	Outlier 11.50 ± 0.25	eV	NIST
IE	11.90	eV	NIST
IE	11.85 ± 0.01	eV	NIST
IE	11.85	eV	NIST
IE	11.84 ± 0.02	eV	NIST
log10WS	[0.28; 0.28]
log10WS	0.28		Aq. Solubility Prediction
log10WS	0.28		Estimated Solubility
logPoct/wat	0.920		Crippen Calculated Property
McVol	54.510	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	4		KDB
NFPA Safety	1		KDB
Pc	[4174.59; 4260.00]	kPa
Pc	4260.00	kPa	KDB
Pc	4260.00 ± 10.00	kPa	NIST
Pc	4180.00 ± 91.19	kPa	NIST
Pc	4174.59 ± 81.06	kPa	NIST
Pc	4194.85 ± 81.06	kPa	NIST
Inp	[510.00; 592.00]
Inp	543.33		NIST
Inp	543.83		NIST
Inp	544.44		NIST
Inp	545.05		NIST
Inp	545.79		NIST
Inp	546.65		NIST
Inp	547.65		NIST
Inp	548.60		NIST
Inp	549.63		NIST
Inp	550.75		NIST
Inp	543.13		NIST
Inp	542.69		NIST
Inp	542.41		NIST
Inp	542.29		NIST
Inp	542.32		NIST
Inp	542.38		NIST
Inp	542.60		NIST
Inp	542.90		NIST
Inp	Outlier 592.00		NIST
Inp	545.30		NIST
Inp	523.00		NIST
Inp	527.00		NIST
Inp	547.00		NIST
Inp	533.00		NIST
Inp	524.00		NIST
Inp	Outlier 510.00		NIST
Inp	573.70		NIST
Inp	554.00		NIST
Inp	554.00		NIST
Inp	555.00		NIST
Inp	557.00		NIST
Inp	544.00		NIST
Inp	524.00		NIST
Inp	539.00		NIST
Inp	542.00		NIST
Inp	539.00		NIST
Inp	Outlier 580.00		NIST
Inp	Outlier 580.00		NIST
Inp	524.00		NIST
Inp	Outlier 580.00		NIST
Inp	554.00		NIST
I	[1015.00; 1046.00]
I	1023.00		NIST
I	1046.00		NIST
I	1015.00		NIST
S°liquid	189.33	J/mol×K	NIST
Tboil	[365.00; 391.70]	K
Tboil	370.29	K	KDB
Tboil	370.50	K	NIST
Tboil	371.00	K	NIST
Tboil	370.45 ± 0.50	K	NIST
Tboil	370.50 ± 0.30	K	NIST
Tboil	370.50 ± 0.30	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.48 ± 0.20	K	NIST
Tboil	370.00 ± 1.50	K	NIST
Tboil	369.00 ± 1.50	K	NIST
Tboil	371.00 ± 1.50	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	369.70 ± 2.00	K	NIST
Tboil	370.50 ± 0.07	K	NIST
Tboil	370.15 ± 1.50	K	NIST
Tboil	Outlier 390.00 ± 3.00	K	NIST
Tboil	368.00 ± 2.00	K	NIST
Tboil	370.00 ± 2.00	K	NIST
Tboil	370.29 ± 0.30	K	NIST
Tboil	369.80 ± 0.40	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	369.00 ± 2.00	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.00 ± 0.40	K	NIST
Tboil	370.00 ± 2.00	K	NIST
Tboil	370.30 ± 0.30	K	NIST
Tboil	370.40 ± 0.10	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	365.00 ± 5.00	K	NIST
Tboil	370.80 ± 0.70	K	NIST
Tboil	370.80 ± 0.60	K	NIST
Tboil	371.00 ± 2.00	K	NIST
Tboil	370.31 ± 0.40	K	NIST
Tboil	371.40 ± 1.00	K	NIST
Tboil	Outlier 391.70 ± 2.00	K	NIST
Tc	[558.70; 561.30]	K
Tc	561.30	K	KDB
Tc	561.30 ± 0.20	K	NIST
Tc	558.70 ± 2.00	K	NIST
Tc	558.85 ± 1.00	K	NIST
Tc	558.85 ± 1.00	K	NIST
Tfus	[171.15; 182.00]	K
Tfus	180.26	K	KDB
Tfus	180.59	K	Aq. Solubility Prediction
Tfus	180.30 ± 0.60	K	NIST
Tfus	180.26 ± 0.10	K	NIST
Tfus	181.15 ± 0.50	K	NIST
Tfus	182.00 ± 2.00	K	NIST
Tfus	181.25 ± 0.20	K	NIST
Tfus	Outlier 171.15 ± 6.00	K	NIST
Tfus	181.30 ± 0.20	K	NIST
Tfus	181.30 ± 0.20	K	NIST
Ttriple	180.37 ± 0.02	K	NIST
Vc	0.229	m3/kmol	KDB
Zc	0.2090320		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[86.00; 112.00]	J/mol×K	[370.12; 563.45]
Cp,gas	86.00	J/mol×K	370.12	Joback Calculated Property
Cp,gas	90.77	J/mol×K	402.34	Joback Calculated Property
Cp,gas	95.36	J/mol×K	434.56	Joback Calculated Property
Cp,gas	99.78	J/mol×K	466.78	Joback Calculated Property
Cp,gas	104.02	J/mol×K	499.00	Joback Calculated Property
Cp,gas	108.09	J/mol×K	531.23	Joback Calculated Property
Cp,gas	112.00	J/mol×K	563.45	Joback Calculated Property
Cp,liquid	[105.30; 119.50]	J/mol×K	[297.00; 303.15]
Cp,liquid	112.90	J/mol×K	297.00	NIST
Cp,liquid	105.30	J/mol×K	298.15	NIST
Cp,liquid	119.50	J/mol×K	298.15	NIST
Cp,liquid	106.00	J/mol×K	303.15	NIST
η	[0.0003822; 0.0004107]	Pa×s	[298.15; 308.15]
η	0.0004107	Pa×s	298.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
η	0.0003991	Pa×s	303.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
η	0.0003822	Pa×s	308.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
ΔfusH	[5.03; 17.07]	kJ/mol	[177.00; 180.40]
ΔfusH	17.07	kJ/mol	177.00	NIST
ΔfusH	5.03	kJ/mol	180.40	NIST
ΔfusH	5.03	kJ/mol	180.40	NIST
ΔvapH	[31.81; 36.70]	kJ/mol	[242.00; 371.00]
ΔvapH	36.50	kJ/mol	242.00	NIST
ΔvapH	36.12	kJ/mol	298.15	NIST
ΔvapH	36.10	kJ/mol	329.50	NIST
ΔvapH	36.70	kJ/mol	335.50	NIST
ΔvapH	35.90	kJ/mol	339.00	NIST
ΔvapH	32.26	kJ/mol	370.30	KDB
ΔvapH	31.81	kJ/mol	371.00	NIST
Pvap	[9.47; 103.78]	kPa	[307.78; 371.23]
Pvap	9.47	kPa	307.78	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	10.59	kPa	309.38	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	11.55	kPa	311.56	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	11.90	kPa	312.50	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	11.90	kPa	312.58	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	12.50	kPa	313.15	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	12.55	kPa	313.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	14.14	kPa	315.89	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	15.71	kPa	318.35	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	17.22	kPa	320.51	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	17.40	kPa	322.00	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	18.58	kPa	322.25	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	19.22	kPa	323.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	21.35	kPa	325.74	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	21.46	kPa	325.79	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	23.64	kPa	328.27	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	26.11	kPa	330.82	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	27.73	kPa	332.31	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	28.57	kPa	333.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	31.64	kPa	335.82	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	34.61	kPa	338.22	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	37.95	kPa	340.70	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	41.33	kPa	343.08	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	46.11	kPa	346.17	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	49.32	kPa	348.09	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	50.91	kPa	349.02	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	54.93	kPa	351.26	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	58.60	kPa	353.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	59.51	kPa	353.63	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	64.72	kPa	356.17	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	69.60	kPa	358.33	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	69.91	kPa	358.53	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	75.34	kPa	360.86	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	80.76	kPa	363.02	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	80.66	kPa	363.10	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	84.93	kPa	364.69	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	91.88	kPa	367.21	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	96.66	kPa	368.88	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	103.78	kPa	371.23	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
n0	[1.36330; 1.36368]		[298.15; 298.15]
n0	1.36330		298.15	Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
n0	1.36368		298.15	Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
ρl	[776.70; 782.00]	kg/m3	[293.00; 298.15]
ρl	782.00	kg/m3	293.00	KDB
ρl	776.70	kg/m3	298.15	Speed of sound as a function of temperature and pressure for propane derivatives
ρl	777.69	kg/m3	298.15	Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
ΔfusS	[9.67; 27.91]	J/mol×K	[177.00; 180.40]
ΔfusS	9.67	J/mol×K	177.00	NIST
ΔfusS	27.91	J/mol×K	180.40	NIST
γ	[0.03; 0.03]	N/m	[293.20; 298.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
ΔvapS	121.10	J/mol×K	298.15	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4308.85]	kPa	[275.44; 564.40]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.42491e+01
Coefficient B			-2.93590e+03
Coefficient C			-6.51540e+01
Temperature range, min.			275.44
Temperature range, max.			564.40
Pvap	1.33	kPa	275.44	Calculated Property
Pvap	8.47	kPa	307.55	Calculated Property
Pvap	34.94	kPa	339.65	Calculated Property
Pvap	107.08	kPa	371.76	Calculated Property
Pvap	265.41	kPa	403.87	Calculated Property
Pvap	562.15	kPa	435.97	Calculated Property
Pvap	1056.42	kPa	468.08	Calculated Property
Pvap	1808.77	kPa	500.19	Calculated Property
Pvap	2876.26	kPa	532.29	Calculated Property
Pvap	4308.85	kPa	564.40	Calculated Property
Pvap	[1.71e-04; 4315.21]	kPa	[180.26; 564.40]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.95302e+01
Coefficient B			-6.51183e+03
Coefficient C			-8.13958e+00
Coefficient D			6.11437e-06
Temperature range, min.			180.26
Temperature range, max.			564.40
Pvap	1.71e-04	kPa	180.26	Calculated Property
Pvap	0.03	kPa	222.94	Calculated Property
Pvap	1.01	kPa	265.62	Calculated Property
Pvap	10.40	kPa	308.31	Calculated Property
Pvap	56.07	kPa	350.99	Calculated Property
Pvap	200.01	kPa	393.67	Calculated Property
Pvap	541.92	kPa	436.35	Calculated Property
Pvap	1216.91	kPa	479.04	Calculated Property
Pvap	2398.54	kPa	521.72	Calculated Property
Pvap	4315.21	kPa	564.40	Calculated Property

Similar Compounds

Find more compounds similar to Propanenitrile.

Mixtures

• Butane + Propanenitrile
• 1-Butene + Propanenitrile
• 1-Propene, 2-methyl- + Propanenitrile
• Propanenitrile + Isobutane
• Propanenitrile + Propane, 2-ethoxy-2-methyl-
• Propanenitrile + Methyl Alcohol
• Ethanol + Propanenitrile
• 1-Propanol + Propanenitrile
• Isopropyl Alcohol + Propanenitrile
• Propanenitrile + 1-Butanol
• Propanenitrile + 1-Pentanol
• Toluene + Propanenitrile
• Acetonitrile + Propanenitrile
• Propanenitrile + Water
• Propanenitrile + 1-Octanol
• Propanenitrile + 1-Decanol
• 1-Undecanol + Propanenitrile
• Butanoic acid, methyl ester + Propanenitrile
• Propanenitrile + Methyl valerate
• Propanenitrile + Hexanoic acid, methyl ester

Find more mixtures with Propanenitrile.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Speed of sound as a function of temperature and pressure for propane derivatives
• Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
• Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
• Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
• Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.