Chemical Properties of 2-Butyne (CAS 503-17-3)

InChI

InChI=1S/C4H6/c1-3-4-2/h1-2H3

InChI Key

XNMQEEKYCVKGBD-UHFFFAOYSA-N

Formula

C4H6

SMILES

CC#CC

Molecular Weight¹

54.09

CAS

503-17-3

Other Names

• But-2-yne
• CH3C«equiv»CCH3
• Crotonylene
• Dimethylacetylene
• UN 1144

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas 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_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : 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_subH : Enthalpy of sublimation 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).
• 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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-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).
• 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	[0.1078; 0.2385]
ω	0.1078		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2385		ChemSep v8.3 pure component data Compiled value
ω	0.1305		KDB
PAff	775.80	kJ/mol	NIST
BasG	745.10	kJ/mol	NIST
ΔcH°gas	-2576.70 ± 0.96	kJ/mol	NIST
μ	[0.80; 3.96]	debye
μ	3.96	debye	ChemSep v8.3 pure component data Compiled value
μ	0.80	debye	KDB
ΔfG°	[184.90; 185.60]	kJ/mol
ΔfG°	184.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	185.60	kJ/mol	KDB
Δc,grossH	2550.94	kJ/mol	KDB
Δc,netH	2418.896	kJ/mol	KDB
ΔfH°gas	[145.10; 148.00]	kJ/mol
ΔfH°gas	145.76 ± 0.79	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	145.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	146.40	kJ/mol	KDB
ΔfH°gas	145.10 ± 1.00	kJ/mol	NIST
ΔfH°gas	148.00 ± 1.50	kJ/mol	NIST
ΔfusH°	9.24	kJ/mol	Joback Calculated Property
ΔvapH°	26.70	kJ/mol	NIST
IE	[9.56; 9.79]	eV
IE	9.58 ± 0.02	eV	NIST
IE	9.59 ± 0.02	eV	NIST
IE	9.56 ± 0.01	eV	NIST
IE	9.61	eV	NIST
IE	9.59	eV	NIST
IE	9.56	eV	NIST
IE	Outlier 9.79	eV	NIST
logPoct/wat	1.030		Crippen Calculated Property
McVol	58.620	ml/mol	McGowan Calculated Property
Pc	[4870.00; 5080.00]	kPa
Pc	4900.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4870.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5080.00	kPa	KDB
Ptriple	6.12	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[462.00; 488.00]
Inp	463.00		NIST
Inp	463.00		NIST
Inp	463.00		NIST
Inp	462.00		NIST
Inp	473.00		NIST
Inp	488.00		NIST
Inp	478.00		NIST
Inp	485.00		NIST
Inp	466.00		NIST
Inp	482.00		NIST
Inp	463.00		NIST
Inp	482.00		NIST
S°liquid	195.10	J/mol×K	NIST
Tboil	[298.65; 301.65]	K
Tboil	300.13	K	ChemSep v8.3 pure component data Compiled value
Tboil	300.12	K	KDB
Tboil	300.00	K	NIST
Tboil	300.20	K	NIST
Tboil	300.12 ± 0.20	K	NIST
Tboil	300.10 ± 0.15	K	NIST
Tboil	300.65 ± 0.50	K	NIST
Tboil	300.13 ± 0.20	K	NIST
Tboil	300.10 ± 0.30	K	NIST
Tboil	300.13 ± 0.30	K	NIST
Tboil	300.11 ± 0.20	K	NIST
Tboil	300.14 ± 0.20	K	NIST
Tboil	300.23 ± 0.30	K	NIST
Tboil	300.14 ± 0.20	K	NIST
Tboil	299.84 ± 0.15	K	NIST
Tboil	300.00 ± 2.00	K	NIST
Tboil	300.35 ± 0.50	K	NIST
Tboil	300.40 ± 1.00	K	NIST
Tboil	300.65 ± 2.00	K	NIST
Tboil	301.15 ± 1.00	K	NIST
Tboil	300.25 ± 0.40	K	NIST
Tboil	Outlier 301.65 ± 1.50	K	NIST
Tboil	Outlier 298.65 ± 3.00	K	NIST
Tboil	300.55 ± 1.00	K	NIST
Tboil	Outlier 301.65 ± 5.00	K	NIST
Tc	[473.20; 488.70]	K
Tc	488.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	473.20	K	ChemSep v8.3 pure component data Compiled value
Tc	488.70	K	KDB
Tfus	[240.50; 241.15]	K
Tfus	241.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	240.91	K	ChemSep v8.3 pure component data Compiled value
Tfus	240.79	K	KDB
Tfus	240.82 ± 0.20	K	NIST
Tfus	240.90 ± 0.20	K	NIST
Tfus	240.63 ± 0.30	K	NIST
Tfus	240.83 ± 0.10	K	NIST
Tfus	240.50 ± 0.30	K	NIST
Ttriple	[240.80; 240.94]	K
Ttriple	240.94	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	240.91	K	ChemSep v8.3 pure component data Compiled value
Ttriple	240.80 ± 0.15	K	NIST
Ttriple	240.93 ± 0.06	K	NIST
Ttriple	240.80 ± 0.15	K	NIST
Ttriple	240.93 ± 0.06	K	NIST
UQi	2.48		ChemSep v8.3 pure component data Compiled value
URi	2.86		ChemSep v8.3 pure component data Compiled value
Vc	[0.221; 0.221]	m3/kmol
Vc	0.221	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.221	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.221	m3/kmol	KDB
VCOSTALD	0.22	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.16		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2740000; 0.2762980]
Zc	0.2740000		ChemSep v8.3 pure component data Compiled value
Zc	0.2762980		KDB
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[84.56; 89.66]	J/mol×K	[336.07; 369.46]
Cp,gas	84.56	J/mol×K	336.07	NIST
Cp,gas	89.66	J/mol×K	369.46	NIST
Cp,liquid	[119.20; 125.10]	J/mol×K	[250.00; 298.15]
Cp,liquid	119.20	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	120.50	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	121.70	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	122.10	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	122.90	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.10	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.14	J/mol×K	290.00	NIST
Cp,liquid	125.10	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[9.23; 9.25]	kJ/mol	[240.90; 240.93]
ΔfusH	9.25	kJ/mol	240.90	NIST
ΔfusH	9.25	kJ/mol	240.90	NIST
ΔfusH	9.23	kJ/mol	240.92	NIST
ΔfusH	9.23	kJ/mol	240.92	NIST
ΔfusH	9.23	kJ/mol	240.93	NIST
ΔsubH	37.40	kJ/mol	219.50	NIST
ΔvapH	[26.65; 29.00]	kJ/mol	[274.00; 300.10]
ΔvapH	29.00	kJ/mol	274.00	NIST
ΔvapH	26.95	kJ/mol	291.00	NIST
ΔvapH	26.95	kJ/mol	291.00	NIST
ΔvapH	26.90 ± 0.30	kJ/mol	291.00	NIST
ΔvapH	26.90 ± 0.10	kJ/mol	291.00	NIST
ΔvapH	26.95	kJ/mol	291.00	NIST
ΔvapH	26.90 ± 0.10	kJ/mol	291.00	NIST
ΔvapH	26.65	kJ/mol	300.10	KDB
n0	1.38930		298.15	KDB
ρl	691.00	kg/m3	293.00	KDB
ΔfusS	[38.33; 38.35]	J/mol×K	[240.92; 240.93]
ΔfusS	38.35	J/mol×K	240.92	NIST
ΔfusS	38.35	J/mol×K	240.92	NIST
ΔfusS	38.33	J/mol×K	240.93	NIST
γ	0.02	N/m	298.20	KDB
ΔvapS	[92.59; 92.59]	J/mol×K	[291.00; 291.00]
ΔvapS	92.59	J/mol×K	291.00	NIST
ΔvapS	92.59	J/mol×K	291.00	NIST
ΔvapS	92.59	J/mol×K	291.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[66.43; 191.74]	J/mol×K	[200.00; 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			6.22260e+01
Coefficient B			-8.26040e+02
Coefficient C			5.60524e+00
Coefficient D			-2.01300e-04
Coefficient E			4.94240e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	66.43	J/mol×K	200.00	Calculated Property
Cp,gas	85.41	J/mol×K	344.44	Calculated Property
Cp,gas	108.24	J/mol×K	488.89	Calculated Property
Cp,gas	128.47	J/mol×K	633.33	Calculated Property
Cp,gas	145.03	J/mol×K	777.78	Calculated Property
Cp,gas	158.38	J/mol×K	922.22	Calculated Property
Cp,gas	169.17	J/mol×K	1066.67	Calculated Property
Cp,gas	178.03	J/mol×K	1211.11	Calculated Property
Cp,gas	185.43	J/mol×K	1355.56	Calculated Property
Cp,gas	191.74	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[119.39; 146.00]	J/mol×K	[240.91; 416.29]	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			1.16500e+02
Coefficient B			3.51160e+01
Coefficient C			-1.04436e+00
Coefficient D			4.98770e-03
Coefficient E			1.30870e-05
Temperature range, min.			240.91
Temperature range, max.			416.29
Cp,liquid	119.39	J/mol×K	240.91	Calculated Property
Cp,liquid	120.08	J/mol×K	260.40	Calculated Property
Cp,liquid	120.99	J/mol×K	279.88	Calculated Property
Cp,liquid	122.19	J/mol×K	299.37	Calculated Property
Cp,liquid	123.79	J/mol×K	318.86	Calculated Property
Cp,liquid	125.94	J/mol×K	338.34	Calculated Property
Cp,liquid	128.86	J/mol×K	357.83	Calculated Property
Cp,liquid	132.84	J/mol×K	377.32	Calculated Property
Cp,liquid	138.34	J/mol×K	396.80	Calculated Property
Cp,liquid	146.00	J/mol×K	416.29	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0003796; 0.0000985]	Pa×s	[240.91; 400.00]	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			-4.56220e-02
Coefficient B			3.05040e+02
Coefficient C			-1.65820e+00
Coefficient D			-4.74900e-08
Coefficient E			2.00000e+00
Temperature range, min.			240.91
Temperature range, max.			400.00
η	0.0003796	Pa×s	240.91	Calculated Property
η	0.0003094	Pa×s	258.59	Calculated Property
η	0.0002570	Pa×s	276.26	Calculated Property
η	0.0002169	Pa×s	293.94	Calculated Property
η	0.0001855	Pa×s	311.62	Calculated Property
η	0.0001605	Pa×s	329.29	Calculated Property
η	0.0001403	Pa×s	346.97	Calculated Property
η	0.0001238	Pa×s	364.65	Calculated Property
η	0.0001100	Pa×s	382.32	Calculated Property
η	0.0000985	Pa×s	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.68]	kPa	[225.64; 319.22]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36731e+01
Coefficient B			-2.08471e+03
Coefficient C			-6.98960e+01
Temperature range, min.			225.64
Temperature range, max.			319.22
Pvap	1.33	kPa	225.64	Calculated Property
Pvap	3.08	kPa	236.04	Calculated Property
Pvap	6.45	kPa	246.44	Calculated Property
Pvap	12.44	kPa	256.83	Calculated Property
Pvap	22.39	kPa	267.23	Calculated Property
Pvap	38.00	kPa	277.63	Calculated Property
Pvap	61.31	kPa	288.03	Calculated Property
Pvap	94.71	kPa	298.42	Calculated Property
Pvap	140.86	kPa	308.82	Calculated Property
Pvap	202.68	kPa	319.22	Calculated Property
Pvap	[4.32; 4872.79]	kPa	[235.35; 473.20]	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			5.96533e+01
Coefficient B			-4.99805e+03
Coefficient C			-6.83428e+00
Coefficient D			6.68205e-06
Coefficient E			2.00000e+00
Temperature range, min.			235.35
Temperature range, max.			473.20
Pvap	4.32	kPa	235.35	Calculated Property
Pvap	19.47	kPa	261.78	Calculated Property
Pvap	64.02	kPa	288.21	Calculated Property
Pvap	167.79	kPa	314.63	Calculated Property
Pvap	371.75	kPa	341.06	Calculated Property
Pvap	725.71	kPa	367.49	Calculated Property
Pvap	1286.21	kPa	393.92	Calculated Property
Pvap	2115.79	kPa	420.34	Calculated Property
Pvap	3284.40	kPa	446.77	Calculated Property
Pvap	4872.79	kPa	473.20	Calculated Property
Pvap	[5.80; 5090.63]	kPa	[240.00; 488.15]	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			4.50165e+01
Coefficient B			-4.55895e+03
Coefficient C			-4.44326e+00
Coefficient D			1.52939e-06
Coefficient E			0.00000e+00
Temperature range, min.			240.00
Temperature range, max.			488.15
Pvap	5.80	kPa	240.00	Calculated Property
Pvap	25.86	kPa	267.57	Calculated Property
Pvap	84.13	kPa	295.14	Calculated Property
Pvap	217.30	kPa	322.72	Calculated Property
Pvap	472.17	kPa	350.29	Calculated Property
Pvap	898.81	kPa	377.86	Calculated Property
Pvap	1543.30	kPa	405.43	Calculated Property
Pvap	2442.34	kPa	433.01	Calculated Property
Pvap	3620.61	kPa	460.58	Calculated Property
Pvap	5090.63	kPa	488.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[744.64; 402.82]	kg/m3	[240.91; 460.97]	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			6.33778e+01
Coefficient B			2.58950e-01
Coefficient C			4.73200e+02
Coefficient D			2.72890e-01
Temperature range, min.			240.91
Temperature range, max.			460.97
ρl	744.64	kg/m3	240.91	Calculated Property
ρl	720.28	kg/m3	265.36	Calculated Property
ρl	694.64	kg/m3	289.81	Calculated Property
ρl	667.44	kg/m3	314.26	Calculated Property
ρl	638.26	kg/m3	338.71	Calculated Property
ρl	606.48	kg/m3	363.17	Calculated Property
ρl	571.08	kg/m3	387.62	Calculated Property
ρl	530.17	kg/m3	412.07	Calculated Property
ρl	479.44	kg/m3	436.52	Calculated Property
ρl	402.82	kg/m3	460.97	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 3.84e-04]	N/m	[240.91; 473.20]	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			-2.82080e-03
Coefficient B			1.16280e+03
Coefficient C			-1.49950e+01
Coefficient D			4.22510e-02
Coefficient E			-5.89440e-05
Comment			Range stopped at Tc; ChemSep gives it to 488.68 K.
Temperature range, min.			240.91
Temperature range, max.			473.20
γ	0.03	N/m	240.91	Calculated Property
γ	0.03	N/m	266.72	Calculated Property
γ	0.02	N/m	292.53	Calculated Property
γ	0.02	N/m	318.34	Calculated Property
γ	0.01	N/m	344.15	Calculated Property
γ	0.01	N/m	369.96	Calculated Property
γ	0.01	N/m	395.77	Calculated Property
γ	0.00	N/m	421.58	Calculated Property
γ	0.00	N/m	447.39	Calculated Property
γ	3.84e-04	N/m	473.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[240.91; 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			2.14970e-04
Coefficient B			9.19980e-01
Coefficient C			2.14540e+02
Coefficient D			1.30500e+05
Temperature range, min.			240.91
Temperature range, max.			1000.00
λgas	0.01	W/m×K	240.91	Calculated Property
λgas	0.02	W/m×K	325.25	Calculated Property
λgas	0.02	W/m×K	409.60	Calculated Property
λgas	0.03	W/m×K	493.94	Calculated Property
λgas	0.04	W/m×K	578.28	Calculated Property
λgas	0.05	W/m×K	662.63	Calculated Property
λgas	0.06	W/m×K	746.97	Calculated Property
λgas	0.07	W/m×K	831.31	Calculated Property
λgas	0.08	W/m×K	915.66	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.08]	W/m×K	[240.91; 428.44]	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			7.44310e-03
Coefficient B			-1.54130e+02
Coefficient C			-2.50980e-01
Coefficient D			-4.62920e-03
Coefficient E			-7.36620e-08
Temperature range, min.			240.91
Temperature range, max.			428.44
λliquid	0.14	W/m×K	240.91	Calculated Property
λliquid	0.14	W/m×K	261.75	Calculated Property
λliquid	0.13	W/m×K	282.58	Calculated Property
λliquid	0.12	W/m×K	303.42	Calculated Property
λliquid	0.11	W/m×K	324.26	Calculated Property
λliquid	0.11	W/m×K	345.09	Calculated Property
λliquid	0.10	W/m×K	365.93	Calculated Property
λliquid	0.09	W/m×K	386.77	Calculated Property
λliquid	0.09	W/m×K	407.60	Calculated Property
λliquid	0.08	W/m×K	428.44	Calculated Property

Similar Compounds

Find more compounds similar to 2-Butyne.

Sources

• KDB Vapor Pressure Data
• 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.
• 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
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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