Chemical Properties of 1-Heptadecene (CAS 6765-39-5)

InChI

InChI=1S/C17H34/c1-3-5-7-9-11-13-15-17-16-14-12-10-8-6-4-2/h3H,1,4-17H2,2H3

InChI Key

ADOBXTDBFNCOBN-UHFFFAOYSA-N

Formula

C17H34

SMILES

C=CCCCCCCCCCCCCCCC

Molecular Weight¹

238.45

CAS

6765-39-5

Other Names

• HEXAHYDROAPLOTAXENE
• Heptadec-1-ene
• Heptadecene-
• NSC 77132

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• 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 standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (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	0.6890		KDB
ΔfG°	180.10	kJ/mol	Joback Calculated Property
ΔfH°gas	-268.78	kJ/mol	Joback Calculated Property
ΔfusH°	38.51	kJ/mol	Joback Calculated Property
ΔvapH°	84.90	kJ/mol	NIST
log10WS	-6.79		Crippen Calculated Property
logPoct/wat	6.654		Crippen Calculated Property
McVol	246.090	ml/mol	McGowan Calculated Property
Pc	1260.00	kPa	KDB
Inp	[1673.00; 1703.00]
Inp	1689.00		NIST
Inp	1698.00		NIST
Inp	1690.00		NIST
Inp	1686.80		NIST
Inp	1687.60		NIST
Inp	Outlier 1703.00		NIST
Inp	1690.00		NIST
Inp	1692.00		NIST
Inp	Outlier 1673.00		NIST
Inp	1692.00		NIST
Inp	1682.00		NIST
Inp	1692.00		NIST
Inp	1687.00		NIST
Inp	1696.00		NIST
Inp	1680.00		NIST
Inp	1700.00		NIST
Inp	1694.00		NIST
Inp	1694.00		NIST
Inp	Outlier 1679.00		NIST
Inp	1691.00		NIST
Inp	1690.00		NIST
Inp	1689.00		NIST
Inp	1692.00		NIST
Inp	1693.90		NIST
Inp	1692.00		NIST
Inp	1683.00		NIST
Inp	1700.00		NIST
Inp	1689.00		NIST
Inp	1693.00		NIST
Inp	1690.00		NIST
Inp	1690.00		NIST
Inp	1690.00		NIST
Inp	1690.00		NIST
Inp	1696.00		NIST
Inp	1692.00		NIST
Inp	1690.00		NIST
Inp	1693.00		NIST
Inp	1687.00		NIST
Inp	1695.00		NIST
I	[1719.00; 1762.00]
I	1762.00		NIST
I	1755.00		NIST
I	1726.00		NIST
I	1724.60		NIST
I	1751.00		NIST
I	1721.00		NIST
I	1746.00		NIST
I	1745.00		NIST
I	1750.00		NIST
I	1746.00		NIST
I	1751.00		NIST
I	1719.00		NIST
Tboil	[573.20; 573.20]	K
Tboil	573.20	K	KDB
Tboil	573.20	K	NIST
Tc	732.40	K	KDB
Tfus	[283.85; 284.00]	K
Tfus	284.00	K	KDB
Tfus	283.85 ± 0.50	K	NIST
Tfus	284.00 ± 2.00	K	NIST
Tfus	284.00 ± 2.00	K	NIST
Vc	0.991	m3/kmol	KDB
Zc	0.2049460		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[645.34; 749.39]	J/mol×K	[585.04; 745.70]
T(K) Ideal gas heat capacity (J/mol×K) 640 660 680 700 720 740 600 650 700
Cp,gas	645.34	J/mol×K	585.04	Joback Calculated Property
Cp,gas	664.54	J/mol×K	611.82	Joback Calculated Property
Cp,gas	682.97	J/mol×K	638.59	Joback Calculated Property
Cp,gas	700.64	J/mol×K	665.37	Joback Calculated Property
Cp,gas	717.59	J/mol×K	692.15	Joback Calculated Property
Cp,gas	733.83	J/mol×K	718.92	Joback Calculated Property
Cp,gas	749.39	J/mol×K	745.70	Joback Calculated Property
η	[0.0001422; 0.0044659]	Pa×s	[279.59; 585.04]
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 300 400 500
η	0.0044659	Pa×s	279.59	Joback Calculated Property
η	0.0016152	Pa×s	330.50	Joback Calculated Property
η	0.0007664	Pa×s	381.41	Joback Calculated Property
η	0.0004334	Pa×s	432.31	Joback Calculated Property
η	0.0002764	Pa×s	483.22	Joback Calculated Property
η	0.0001921	Pa×s	534.13	Joback Calculated Property
η	0.0001422	Pa×s	585.04	Joback Calculated Property
ΔvapH	[51.84; 72.30]	kJ/mol	[404.00; 672.00]
ΔvapH	72.30	kJ/mol	404.00	NIST
ΔvapH	51.84	kJ/mol	573.20	KDB
ΔvapH	55.50	kJ/mol	672.00	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[431.20; 433.20]	K	[1.30; 1.50]
Tboilr	433.20	K	1.30	NIST
Tboilr	431.20	K	1.50	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[433.23; 595.34]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.56682e+01
Coefficient B			-5.14021e+03
Coefficient C			-9.90300e+01
Temperature range, min.			433.23
Temperature range, max.			595.34
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550
Pvap	1.33	kPa	433.23	Calculated Property
Pvap	2.93	kPa	451.24	Calculated Property
Pvap	5.95	kPa	469.25	Calculated Property
Pvap	11.34	kPa	487.27	Calculated Property
Pvap	20.40	kPa	505.28	Calculated Property
Pvap	34.90	kPa	523.29	Calculated Property
Pvap	57.17	kPa	541.30	Calculated Property
Pvap	90.09	kPa	559.32	Calculated Property
Pvap	137.19	kPa	577.33	Calculated Property
Pvap	202.63	kPa	595.34	Calculated Property
Pvap	[1.05e-05; 1409.57]	kPa	[284.40; 736.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.96918e+02
Coefficient B			-1.78740e+04
Coefficient C			-2.59062e+01
Coefficient D			1.03945e-05
Temperature range, min.			284.40
Temperature range, max.			736.00
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 400 600
Pvap	1.05e-05	kPa	284.40	Calculated Property
Pvap	2.66e-03	kPa	334.58	Calculated Property
Pvap	0.11	kPa	384.76	Calculated Property
Pvap	1.50	kPa	434.93	Calculated Property
Pvap	10.03	kPa	485.11	Calculated Property
Pvap	42.18	kPa	535.29	Calculated Property
Pvap	129.93	kPa	585.47	Calculated Property
Pvap	324.95	kPa	635.64	Calculated Property
Pvap	707.63	kPa	685.82	Calculated Property
Pvap	1409.57	kPa	736.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Heptadecene.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Crippen Method
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
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