Heptane, 2-methyl- (CAS 592-27-8)

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Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3780		KDB
AP	347.150	K	KDB
Δ_cH°_liquid	[-5465.50; -5274.60]	kJ/mol
Δ_cH°_liquid	-5465.50 ± 1.20	kJ/mol	NIST
Δ_cH°_liquid	-5447.10	kJ/mol	NIST
Δ_cH°_liquid	-5274.60	kJ/mol	NIST
Δ_fG°	12.77	kJ/mol	KDB
Δ_c,grossH	5465.48	kJ/mol	KDB
Δ_c,netH	5069.335	kJ/mol	KDB
Δ_fH°_gas	[-215.60; -215.50]	kJ/mol
Δ_fH°_gas	-215.60	kJ/mol	KDB
Δ_fH°_gas	-215.50 ± 1.30	kJ/mol	NIST
Δ_fH°_liquid	-255.20 ± 1.30	kJ/mol	NIST
Δ_fusH°	12.95	kJ/mol	Joback Calculated Property
Δ_vapH°	[33.00; 39.80]	kJ/mol
Δ_vapH°	39.72	kJ/mol	NIST
Δ_vapH°	39.70 ± 0.10	kJ/mol	NIST
Δ_vapH°	39.70	kJ/mol	NIST
Δ_vapH°	39.80 ± 0.10	kJ/mol	NIST
Δ_vapH°	39.67	kJ/mol	NIST
Δ_vapH°	Outlier 33.00	kJ/mol	NIST
IE	[9.74; 9.84]	eV
IE	9.84 ± 0.10	eV	NIST
IE	9.76	eV	NIST
IE	9.84 ± 0.10	eV	NIST
IE	9.74 ± 0.15	eV	NIST
log₁₀WS	[-5.08; -5.08]
log₁₀WS	-5.08		Aq. Solubility Prediction
log₁₀WS	-5.08		Estimated Solubility
logP_oct/wat	3.223		Crippen Calculated Property
McVol	123.580	ml/mol	McGowan Calculated Property
P_c	[2484.20; 2500.00]	kPa
P_c	2500.00	kPa	KDB
P_c	2500.00 ± 20.00	kPa	NIST
P_c	2500.00 ± 40.00	kPa	NIST
P_c	2484.20 ± 40.53	kPa	NIST
ρ_c	[234.17; 234.17]	kg/m³
ρ_c	234.17 ± 2.28	kg/m³	NIST
ρ_c	234.17 ± 4.57	kg/m³	NIST
I_np	[754.00; 778.00]
I_np	765.50		NIST
I_np	765.80		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	766.30		NIST
I_np	765.00		NIST
I_np	767.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	764.70		NIST
I_np	765.60		NIST
I_np	766.00		NIST
I_np	766.20		NIST
I_np	766.30		NIST
I_np	766.30		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	766.50		NIST
I_np	766.40		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	Outlier 754.00		NIST
I_np	764.00		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	765.20		NIST
I_np	764.90		NIST
I_np	765.00		NIST
I_np	764.60		NIST
I_np	764.60		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	Outlier 772.52		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	763.00		NIST
I_np	763.00		NIST
I_np	763.00		NIST
I_np	763.00		NIST
I_np	763.00		NIST
I_np	764.80		NIST
I_np	767.00		NIST
I_np	765.00		NIST
I_np	765.10		NIST
I_np	764.00		NIST
I_np	764.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	764.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	764.50		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	764.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	763.00		NIST
I_np	761.00		NIST
I_np	760.00		NIST
I_np	764.10		NIST
I_np	769.00		NIST
I_np	765.00		NIST
I_np	Outlier 778.00		NIST
I_np	766.90		NIST
I_np	761.38		NIST
I_np	761.79		NIST
I_np	762.50		NIST
I_np	764.10		NIST
I_np	761.00		NIST
I_np	761.10		NIST
I_np	762.25		NIST
I_np	762.36		NIST
I_np	763.00		NIST
I_np	763.03		NIST
I_np	763.50		NIST
I_np	763.00		NIST
I_np	765.90		NIST
I_np	765.50		NIST
I_np	765.50		NIST
I_np	766.78		NIST
I_np	766.99		NIST
I_np	767.12		NIST
I_np	765.99		NIST
I_np	766.21		NIST
I_np	766.26		NIST
I_np	761.00		NIST
I_np	760.00		NIST
I_np	Outlier 776.21		NIST
I_np	764.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	Outlier 756.00		NIST
I_np	767.00		NIST
I_np	763.00		NIST
I_np	767.00		NIST
I_np	764.30		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	Outlier 775.00		NIST
I_np	767.00		NIST
I_np	760.00		NIST
I_np	759.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	768.00		NIST
I_np	765.00		NIST
I_np	765.00		NIST
I_np	Outlier 758.54		NIST
I_np	764.00		NIST
I_np	766.00		NIST
I_np	763.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	766.00		NIST
I_np	762.00		NIST
I_np	761.00		NIST
I_np	766.00		NIST
I_np	Outlier 775.00		NIST
I_np	Outlier 772.00		NIST
I_np	770.00		NIST
I_np	Outlier 772.00		NIST
I_np	760.00		NIST
I_np	766.00		NIST
I_np	765.00		NIST
I_np	764.10		NIST
I_np	759.00		NIST
I_np	Outlier 772.00		NIST
I	[750.00; 764.00]
I	750.00		NIST
I	764.00		NIST
I	764.00		NIST
S°_gas	459.49 ± 0.88	J/mol×K	NIST
S°_liquid	356.39	J/mol×K	NIST
T_boil	[389.15; 391.60]	K
T_boil	390.81	K	KDB
T_boil	390.80	K	NIST
T_boil	390.80	K	NIST
T_boil	391.00 ± 3.00	K	NIST
T_boil	390.00 ± 3.00	K	NIST
T_boil	391.00 ± 2.00	K	NIST
T_boil	390.80 ± 0.20	K	NIST
T_boil	Outlier 391.60 ± 2.00	K	NIST
T_boil	390.79 ± 0.10	K	NIST
T_boil	390.40 ± 0.30	K	NIST
T_boil	390.85 ± 0.20	K	NIST
T_boil	390.78 ± 0.20	K	NIST
T_boil	390.55 ± 0.50	K	NIST
T_boil	390.85 ± 0.30	K	NIST
T_boil	391.00 ± 0.30	K	NIST
T_boil	390.86 ± 0.20	K	NIST
T_boil	390.90 ± 0.15	K	NIST
T_boil	390.90 ± 0.20	K	NIST
T_boil	390.79 ± 0.01	K	NIST
T_boil	390.90 ± 0.20	K	NIST
T_boil	390.85 ± 0.20	K	NIST
T_boil	390.75 ± 0.50	K	NIST
T_boil	390.15 ± 1.00	K	NIST
T_boil	390.15 ± 1.50	K	NIST
T_boil	390.00 ± 3.00	K	NIST
T_boil	390.85 ± 0.10	K	NIST
T_boil	390.80 ± 0.30	K	NIST
T_boil	390.79 ± 0.10	K	NIST
T_boil	391.15 ± 0.30	K	NIST
T_boil	391.25 ± 0.30	K	NIST
T_boil	389.85 ± 0.50	K	NIST
T_boil	Outlier 389.75 ± 0.60	K	NIST
T_boil	390.35 ± 0.60	K	NIST
T_boil	390.35 ± 0.50	K	NIST
T_boil	391.00 ± 1.00	K	NIST
T_boil	390.65 ± 1.50	K	NIST
T_boil	Outlier 389.15 ± 0.30	K	NIST
T_boil	390.90 ± 1.00	K	NIST
T_boil	391.15 ± 1.00	K	NIST
T_c	[559.56; 559.70]	K
T_c	559.70	K	KDB
T_c	559.70 ± 0.10	K	NIST
T_c	559.70 ± 0.20	K	NIST
T_c	559.60	K	NIST
T_c	559.56 ± 0.40	K	NIST
T_c	559.57 ± 0.20	K	NIST
T_fus	[160.00; 165.52]	K
T_fus	164.16	K	KDB
T_fus	165.52	K	Aq. Solubility Prediction
T_fus	163.59 ± 0.20	K	NIST
T_fus	163.59 ± 0.30	K	NIST
T_fus	163.52 ± 0.20	K	NIST
T_fus	163.52 ± 0.30	K	NIST
T_fus	163.90 ± 0.02	K	NIST
T_fus	164.02 ± 0.09	K	NIST
T_fus	164.03 ± 0.06	K	NIST
T_fus	164.11 ± 0.05	K	NIST
T_fus	163.32 ± 0.15	K	NIST
T_fus	163.55 ± 0.50	K	NIST
T_fus	163.65 ± 0.10	K	NIST
T_fus	Outlier 160.00 ± 0.30	K	NIST
T_fus	162.15 ± 2.00	K	NIST
T_fus	161.85 ± 1.50	K	NIST
T_triple	[154.87; 164.19]	K
T_triple	164.18 ± 0.04	K	NIST
T_triple	164.19 ± 0.01	K	NIST
T_triple	163.15 ± 0.02	K	NIST
T_triple	164.14 ± 0.02	K	NIST
T_triple	164.14 ± 0.02	K	NIST
T_triple	164.14 ± 0.40	K	NIST
T_triple	154.91 ± 0.02	K	NIST
T_triple	154.87 ± 0.04	K	NIST
T_triple	154.91 ± 0.03	K	NIST
T_triple	154.87 ± 0.05	K	NIST
V_c	[0.488; 0.488]	m³/kmol
V_c	0.488	m³/kmol	KDB
V_c	0.488	m³/kmol	NIST
Z_c	0.2621610		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[186.13; 265.52]	J/mol×K	[298.15; 448.15]

C_p,gas	186.13	J/mol×K	298.15	NIST
C_p,gas	202.07	J/mol×K	323.15	NIST
C_p,gas	230.06	J/mol×K	373.15	NIST
C_p,gas	248.37	J/mol×K	408.15	NIST
C_p,gas	265.52	J/mol×K	448.15	NIST
C_p,liquid	[251.58; 252.00]	J/mol×K	[298.15; 298.15]
C_p,liquid	252.00	J/mol×K	298.15	NIST
C_p,liquid	251.58	J/mol×K	298.15	NIST
C_sat	[213.20; 288.40]	J/mol×K	[180.00; 370.00]

C_sat	213.20	J/mol×K	180.00	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
C_sat	215.00	J/mol×K	190.00	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
C_sat	217.00	J/mol×K	200.00	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
C_sat	219.40	J/mol×K	210.00	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
C_sat	222.10	J/mol×K	220.00	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
C_sat	225.00	J/mol×K	230.00	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
C_sat	228.20	J/mol×K	240.00	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
C_sat	231.70	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
C_sat	235.40	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
C_sat	239.40	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
C_sat	240.70	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
C_sat	243.60	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
C_sat	247.90	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
C_sat	251.60	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
C_sat	252.50	J/mol×K	300.00	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
C_sat	257.20	J/mol×K	310.00	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
C_sat	262.10	J/mol×K	320.00	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
C_sat	267.10	J/mol×K	330.00	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
C_sat	272.30	J/mol×K	340.00	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
C_sat	277.60	J/mol×K	350.00	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
C_sat	282.90	J/mol×K	360.00	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
C_sat	288.40	J/mol×K	370.00	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
η	[0.0002373; 0.0105616]	Pa×s	[164.92; 382.00]

η	0.0105616	Pa×s	164.92	Joback Calculated Property
η	0.0031758	Pa×s	201.10	Joback Calculated Property
η	0.0013776	Pa×s	237.28	Joback Calculated Property
η	0.0007454	Pa×s	273.46	Joback Calculated Property
η	0.0004656	Pa×s	309.64	Joback Calculated Property
η	0.0003209	Pa×s	345.82	Joback Calculated Property
η	0.0002373	Pa×s	382.00	Joback Calculated Property
Δ_fusH	[11.92; 11.92]	kJ/mol	[64.19; 164.20]
Δ_fusH	11.92	kJ/mol	64.19	NIST
Δ_fusH	11.92	kJ/mol	164.20	NIST
Δ_fusH	11.92	kJ/mol	164.20	NIST
Δ_vapH	[33.26; 41.60]	kJ/mol	[258.00; 390.80]

Δ_vapH	41.60	kJ/mol	258.00	NIST
Δ_vapH	38.70 ± 0.10	kJ/mol	313.00	NIST
Δ_vapH	37.30 ± 0.10	kJ/mol	333.00	NIST
Δ_vapH	39.80	kJ/mol	338.50	NIST
Δ_vapH	36.00 ± 0.10	kJ/mol	353.00	NIST
Δ_vapH	38.10	kJ/mol	353.00	NIST
Δ_vapH	33.81	kJ/mol	390.80	KDB
Δ_vapH	33.26	kJ/mol	390.80	NIST
n₀	1.39257		298.15	KDB
ρ_l	702.00	kg/m³	289.00	KDB
Δ_fusS	72.60	J/mol×K	64.19	NIST
γ	0.02	N/m	298.20	KDB
λ	[0.11; 0.12]	W/m×K	[259.12; 328.23]

λ	0.12	W/m×K	259.12	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	259.33	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	259.51	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	277.53	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	277.77	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	277.96	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	295.72	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	295.95	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	296.16	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	313.83	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	314.07	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	314.30	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	327.74	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	328.00	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	328.23	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
V_m	[1.63e-04; 1.64e-04]	m³/mol	[288.05; 298.15]
V_m	1.63e-04	m³/mol	288.05	Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
V_m	1.64e-04	m³/mol	298.15	Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	389.20	K	101.00	NIST

Datasets

Molar heat capacity at constant pressure, J/K/mol (1)
Mass density, kg/m3 (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	100.00	236.20
293.15	5000.00	233.80
293.15	10000.00	231.70
293.15	15000.00	229.10
293.15	20000.00	228.00
293.15	25000.00	224.80
313.15	100.00	249.60
313.15	5000.00	246.80
313.15	10000.00	245.10
313.15	15000.00	243.20
313.15	20000.00	240.80
313.15	25000.00	235.10
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	693.9
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.63]	kPa	[284.25; 417.28]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.43957e+01
Coefficient B			-3.39364e+03
Coefficient C			-4.37100e+01
Temperature range, min.			284.25
Temperature range, max.			417.28

P_vap	1.33	kPa	284.25	Calculated Property
P_vap	3.02	kPa	299.03	Calculated Property
P_vap	6.24	kPa	313.81	Calculated Property
P_vap	11.98	kPa	328.59	Calculated Property
P_vap	21.56	kPa	343.37	Calculated Property
P_vap	36.72	kPa	358.16	Calculated Property
P_vap	59.61	kPa	372.94	Calculated Property
P_vap	92.83	kPa	387.72	Calculated Property
P_vap	139.37	kPa	402.50	Calculated Property
P_vap	202.63	kPa	417.28	Calculated Property
P_vap	[1.04e-06; 2474.20]	kPa	[164.16; 559.64]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			8.36210e+01
Coefficient B			-7.47230e+03
Coefficient C			-1.02064e+01
Coefficient D			6.78071e-06
Temperature range, min.			164.16
Temperature range, max.			559.64

P_vap	1.04e-06	kPa	164.16	Calculated Property
P_vap	1.54e-03	kPa	208.10	Calculated Property
P_vap	0.13	kPa	252.04	Calculated Property
P_vap	2.44	kPa	295.99	Calculated Property
P_vap	18.77	kPa	339.93	Calculated Property
P_vap	83.36	kPa	383.87	Calculated Property
P_vap	259.37	kPa	427.81	Calculated Property
P_vap	636.04	kPa	471.76	Calculated Property
P_vap	1326.32	kPa	515.70	Calculated Property
P_vap	2474.20	kPa	559.64	Calculated Property

Similar Compounds

Find more compounds similar to Heptane, 2-methyl-.

Mixtures

Sources

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Chemical Properties of Heptane, 2-methyl- (CAS 592-27-8)

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