Pentane, 2,2,4-trimethyl- (CAS 540-84-1)

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Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3030		KDB
AP	352.650	K	KDB
Δ_cH°_liquid	-5461.30 ± 1.30	kJ/mol	NIST
Δ_fG°	13.69	kJ/mol	KDB
R_g	4.1710		KDB
Δ_c,grossH	5461.33	kJ/mol	KDB
Δ_c,netH	5065.192	kJ/mol	KDB
Δ_fH°_gas	[-224.30; -224.10]	kJ/mol
Δ_fH°_gas	-224.30	kJ/mol	KDB
Δ_fH°_gas	-224.10 ± 1.30	kJ/mol	NIST
Δ_fH°_liquid	-259.30 ± 1.30	kJ/mol	NIST
Δ_fusH°	5.54	kJ/mol	Joback Calculated Property
Δ_vapH°	[34.90; 35.24]	kJ/mol
Δ_vapH°	35.24	kJ/mol	NIST
Δ_vapH°	Outlier 34.90	kJ/mol	NIST
Δ_vapH°	35.20 ± 0.10	kJ/mol	NIST
Δ_vapH°	35.10 ± 0.10	kJ/mol	NIST
Δ_vapH°	35.10	kJ/mol	NIST
Δ_vapH°	35.10 ± 0.10	kJ/mol	NIST
Δ_vapH°	35.12	kJ/mol	NIST
IE	[9.86; 9.91]	eV
IE	9.89 ± 0.03	eV	NIST
IE	9.91	eV	NIST
IE	9.86	eV	NIST
log₁₀WS	[-4.74; -4.74]
log₁₀WS	-4.74		Aq. Solubility Prediction
log₁₀WS	-4.74		Estimated Solubility
logP_oct/wat	3.079		Crippen Calculated Property
McVol	123.580	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
P_c	[2564.33; 2583.79]	kPa
P_c	2570.00	kPa	Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
P_c	2570.00	kPa	KDB
P_c	2570.00 ± 20.00	kPa	NIST
P_c	2567.60 ± 40.53	kPa	NIST
P_c	2564.33 ± 10.13	kPa	NIST
P_c	Outlier 2583.79 ± 15.19	kPa	NIST
ρ_c	[243.31; 244.45]	kg/m³
ρ_c	244.45 ± 2.28	kg/m³	NIST
ρ_c	243.31 ± 4.57	kg/m³	NIST
ρ_c	243.31 ± 3.43	kg/m³	NIST
I_np	[680.00; 703.10]
I_np	692.70		NIST
I_np	689.10		NIST
I_np	694.00		NIST
I_np	691.10		NIST
I_np	689.90		NIST
I_np	690.20		NIST
I_np	690.60		NIST
I_np	693.00		NIST
I_np	Outlier 700.00		NIST
I_np	694.90		NIST
I_np	691.00		NIST
I_np	693.50		NIST
I_np	Outlier 697.70		NIST
I_np	Outlier 703.10		NIST
I_np	687.00		NIST
I_np	694.10		NIST
I_np	694.00		NIST
I_np	691.00		NIST
I_np	689.00		NIST
I_np	691.00		NIST
I_np	694.00		NIST
I_np	689.90		NIST
I_np	692.20		NIST
I_np	693.00		NIST
I_np	690.00		NIST
I_np	690.00		NIST
I_np	691.00		NIST
I_np	691.00		NIST
I_np	691.00		NIST
I_np	692.00		NIST
I_np	695.00		NIST
I_np	688.00		NIST
I_np	689.00		NIST
I_np	690.00		NIST
I_np	691.00		NIST
I_np	692.00		NIST
I_np	694.00		NIST
I_np	686.60		NIST
I_np	687.50		NIST
I_np	688.60		NIST
I_np	689.60		NIST
I_np	690.70		NIST
I_np	691.90		NIST
I_np	691.40		NIST
I_np	691.30		NIST
I_np	689.00		NIST
I_np	690.00		NIST
I_np	690.00		NIST
I_np	696.00		NIST
I_np	691.00		NIST
I_np	694.00		NIST
I_np	693.00		NIST
I_np	691.00		NIST
I_np	688.60		NIST
I_np	690.00		NIST
I_np	692.00		NIST
I_np	684.00		NIST
I_np	686.00		NIST
I_np	686.00		NIST
I_np	687.00		NIST
I_np	688.00		NIST
I_np	690.30		NIST
I_np	695.00		NIST
I_np	Outlier 699.00		NIST
I_np	687.00		NIST
I_np	694.00		NIST
I_np	689.00		NIST
I_np	689.00		NIST
I_np	688.00		NIST
I_np	690.00		NIST
I_np	692.00		NIST
I_np	694.00		NIST
I_np	688.00		NIST
I_np	690.00		NIST
I_np	688.00		NIST
I_np	690.00		NIST
I_np	692.00		NIST
I_np	696.00		NIST
I_np	687.00		NIST
I_np	689.00		NIST
I_np	689.00		NIST
I_np	692.00		NIST
I_np	691.00		NIST
I_np	693.00		NIST
I_np	694.00		NIST
I_np	687.00		NIST
I_np	694.00		NIST
I_np	690.00		NIST
I_np	Outlier 680.00		NIST
I_np	686.00		NIST
I_np	685.00		NIST
I_np	688.44		NIST
I_np	689.00		NIST
I_np	687.00		NIST
I_np	687.50		NIST
I_np	683.91		NIST
I_np	688.00		NIST
I_np	687.00		NIST
I_np	686.00		NIST
I_np	686.00		NIST
I_np	684.80		NIST
I_np	691.00		NIST
I_np	688.00		NIST
I_np	690.00		NIST
I_np	695.00		NIST
I_np	692.00		NIST
I_np	693.00		NIST
I_np	689.00		NIST
I_np	689.00		NIST
I_np	691.00		NIST
I_np	691.00		NIST
I_np	684.38		NIST
I_np	689.00		NIST
I_np	689.00		NIST
I_np	689.00		NIST
I_np	690.00		NIST
I_np	694.00		NIST
I_np	690.00		NIST
I_np	691.00		NIST
I_np	692.00		NIST
I_np	691.00		NIST
I_np	688.00		NIST
I_np	688.00		NIST
I_np	692.00		NIST
I_np	685.00		NIST
I_np	685.00		NIST
I_np	692.00		NIST
I_np	686.00		NIST
I_np	Outlier 700.00		NIST
I_np	Outlier 700.00		NIST
I_np	688.44		NIST
I_np	684.80		NIST
I_np	687.00		NIST
I_np	686.00		NIST
I_np	692.70		NIST
I_np	690.20		NIST
I_np	691.00		NIST
I_np	694.10		NIST
I_np	694.00		NIST
I_np	690.00		NIST
I_np	695.00		NIST
I_np	692.00		NIST
I_np	689.60		NIST
I_np	689.00		NIST
I_np	688.00		NIST
I	[676.00; 711.00]
I	676.00		NIST
I	698.00		NIST
I	711.00		NIST
I	705.00		NIST
I	711.00		NIST
S°_liquid	[314.60; 328.03]	J/mol×K
S°_liquid	328.03	J/mol×K	NIST
S°_liquid	314.60	J/mol×K	NIST
T_boil	[371.45; 389.00]	K
T_boil	372.33	K	Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
T_boil	372.33	K	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
T_boil	372.26	K	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
T_boil	372.35	K	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
T_boil	372.37	K	KDB
T_boil	372.40 ± 0.20	K	NIST
T_boil	372.40 ± 0.20	K	NIST
T_boil	372.40	K	NIST
T_boil	372.40	K	NIST
T_boil	372.00 ± 0.15	K	NIST
T_boil	372.40 ± 0.15	K	NIST
T_boil	372.50 ± 0.25	K	NIST
T_boil	372.30 ± 0.30	K	NIST
T_boil	372.15 ± 0.50	K	NIST
T_boil	372.30 ± 0.50	K	NIST
T_boil	372.35 ± 0.30	K	NIST
T_boil	372.39 ± 0.20	K	NIST
T_boil	371.45 ± 0.60	K	NIST
T_boil	372.15 ± 0.40	K	NIST
T_boil	372.30 ± 0.20	K	NIST
T_boil	372.40 ± 0.60	K	NIST
T_boil	372.37 ± 0.20	K	NIST
T_boil	372.38 ± 0.05	K	NIST
T_boil	372.39 ± 0.10	K	NIST
T_boil	372.65 ± 2.00	K	NIST
T_boil	372.15 ± 2.00	K	NIST
T_boil	372.35 ± 0.40	K	NIST
T_boil	372.45 ± 0.30	K	NIST
T_boil	372.50 ± 0.40	K	NIST
T_boil	372.38 ± 0.27	K	NIST
T_boil	372.38 ± 0.20	K	NIST
T_boil	372.38 ± 0.15	K	NIST
T_boil	372.45 ± 0.50	K	NIST
T_boil	372.38 ± 0.10	K	NIST
T_boil	372.38 ± 0.01	K	NIST
T_boil	372.39 ± 0.25	K	NIST
T_boil	372.38 ± 0.10	K	NIST
T_boil	372.45 ± 0.50	K	NIST
T_boil	372.39 ± 0.07	K	NIST
T_boil	372.50 ± 0.20	K	NIST
T_boil	372.55 ± 0.20	K	NIST
T_boil	372.39 ± 0.05	K	NIST
T_boil	372.38 ± 0.05	K	NIST
T_boil	372.39 ± 0.20	K	NIST
T_boil	372.55 ± 0.30	K	NIST
T_boil	372.38 ± 0.03	K	NIST
T_boil	372.25 ± 0.50	K	NIST
T_boil	372.25 ± 0.20	K	NIST
T_boil	372.38 ± 0.10	K	NIST
T_boil	372.38 ± 0.10	K	NIST
T_boil	372.40 ± 0.40	K	NIST
T_boil	372.25 ± 0.20	K	NIST
T_boil	372.65 ± 2.00	K	NIST
T_boil	372.35 ± 0.50	K	NIST
T_boil	372.45 ± 0.40	K	NIST
T_boil	372.45 ± 0.50	K	NIST
T_boil	Outlier 389.00 ± 2.00	K	NIST
T_c	[543.61; 544.30]	K
T_c	544.00	K	The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
T_c	543.80	K	KDB
T_c	543.80 ± 0.30	K	NIST
T_c	543.90	K	NIST
T_c	543.89 ± 0.40	K	NIST
T_c	543.61 ± 0.20	K	NIST
T_c	543.82 ± 0.10	K	NIST
T_c	Outlier 544.30 ± 0.20	K	NIST
T_fus	[165.00; 166.15]	K
T_fus	165.80	K	KDB
T_fus	Outlier 166.07	K	Aq. Solubility Prediction
T_fus	165.78 ± 0.10	K	NIST
T_fus	165.75 ± 0.04	K	NIST
T_fus	165.76 ± 0.02	K	NIST
T_fus	165.75 ± 0.02	K	NIST
T_fus	165.76 ± 0.02	K	NIST
T_fus	165.73 ± 0.10	K	NIST
T_fus	165.73 ± 0.10	K	NIST
T_fus	165.73 ± 0.10	K	NIST
T_fus	165.73 ± 0.06	K	NIST
T_fus	165.73 ± 0.06	K	NIST
T_fus	165.73 ± 0.06	K	NIST
T_fus	165.77 ± 0.09	K	NIST
T_fus	165.77 ± 0.05	K	NIST
T_fus	165.76 ± 0.06	K	NIST
T_fus	165.76 ± 0.03	K	NIST
T_fus	165.85 ± 0.20	K	NIST
T_fus	165.73 ± 0.10	K	NIST
T_fus	165.76 ± 0.06	K	NIST
T_fus	165.75 ± 0.15	K	NIST
T_fus	165.76 ± 0.03	K	NIST
T_fus	165.77 ± 0.02	K	NIST
T_fus	165.73 ± 0.15	K	NIST
T_fus	165.75 ± 0.30	K	NIST
T_fus	165.75 ± 0.12	K	NIST
T_fus	165.77 ± 0.05	K	NIST
T_fus	165.78 ± 0.03	K	NIST
T_fus	165.75 ± 0.04	K	NIST
T_fus	165.77 ± 0.02	K	NIST
T_fus	165.78 ± 0.20	K	NIST
T_fus	165.75 ± 0.01	K	NIST
T_fus	165.83 ± 0.30	K	NIST
T_fus	165.83 ± 0.30	K	NIST
T_fus	165.75 ± 0.50	K	NIST
T_fus	165.78 ± 0.20	K	NIST
T_fus	165.78 ± 0.07	K	NIST
T_fus	165.55 ± 0.40	K	NIST
T_fus	165.83 ± 0.20	K	NIST
T_fus	165.55 ± 0.20	K	NIST
T_fus	165.84 ± 0.06	K	NIST
T_fus	Outlier 166.15 ± 2.00	K	NIST
T_fus	Outlier 165.00 ± 2.00	K	NIST
T_fus	165.65 ± 0.50	K	NIST
T_fus	165.45 ± 0.40	K	NIST
T_fus	Outlier 165.35 ± 0.50	K	NIST
T_triple	[165.30; 165.76]	K
T_triple	165.76 ± 0.40	K	NIST
T_triple	165.30 ± 0.20	K	NIST
T_triple	165.30 ± 0.20	K	NIST
V_c	[0.468; 0.482]	m³/kmol
V_c	0.468	m³/kmol	KDB
V_c	0.468	m³/kmol	NIST
V_c	0.482 ± 0.020	m³/kmol	NIST
Z_c	0.2660130		KDB
Z_ra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[233.00; 313.27]	J/mol×K	[378.77; 557.09]

C_p,gas	233.00	J/mol×K	378.77	Joback Calculated Property
C_p,gas	248.05	J/mol×K	408.49	Joback Calculated Property
C_p,gas	262.39	J/mol×K	438.21	Joback Calculated Property
C_p,gas	276.06	J/mol×K	467.93	Joback Calculated Property
C_p,gas	289.08	J/mol×K	497.65	Joback Calculated Property
C_p,gas	301.48	J/mol×K	527.37	Joback Calculated Property
C_p,gas	313.27	J/mol×K	557.09	Joback Calculated Property
C_p,liquid	[186.00; 275.50]	J/mol×K	[170.00; 370.00]

C_p,liquid	186.00	J/mol×K	170.00	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_p,liquid	189.20	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_p,liquid	192.60	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_p,liquid	196.20	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_p,liquid	199.90	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_p,liquid	203.80	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_p,liquid	207.80	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_p,liquid	211.90	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_p,liquid	216.20	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
C_p,liquid	220.70	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_p,liquid	225.20	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_p,liquid	226.70	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_p,liquid	229.90	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
C_p,liquid	234.60	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_p,liquid	237.85	J/mol×K	293.15	NIST
C_p,liquid	233.90	J/mol×K	295.20	NIST
C_p,liquid	242.49	J/mol×K	298.15	NIST
C_p,liquid	237.80	J/mol×K	298.15	NIST
C_p,liquid	238.60	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_p,liquid	238.57	J/mol×K	298.15	NIST
C_p,liquid	237.80	J/mol×K	298.15	NIST
C_p,liquid	238.87	J/mol×K	298.15	NIST
C_p,liquid	239.71	J/mol×K	298.15	NIST
C_p,liquid	242.49	J/mol×K	298.15	NIST
C_p,liquid	239.50	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_p,liquid	233.70	J/mol×K	300.00	NIST
C_p,liquid	241.00	J/mol×K	301.90	NIST
C_p,liquid	244.40	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_p,liquid	249.40	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_p,liquid	254.50	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_p,liquid	259.70	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_p,liquid	264.90	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_p,liquid	270.20	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_p,liquid	275.50	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	[0.0003690; 0.0005439]	Pa×s	[288.15; 323.15]

η	0.0005439	Pa×s	288.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0005125	Pa×s	293.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0004844	Pa×s	298.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0004780	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0004586	Pa×s	303.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0004530	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0004216	Pa×s	308.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0004290	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0004130	Pa×s	313.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0004080	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0003880	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0003690	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
Δ_fusH	[9.04; 9.21]	kJ/mol	[165.30; 165.80]

Δ_fusH	9.04	kJ/mol	165.30	NIST
Δ_fusH	9.04	kJ/mol	165.30	NIST
Δ_fusH	9.04	kJ/mol	165.30	NIST
Δ_fusH	9.04	kJ/mol	165.30	NIST
Δ_fusH	9.21	kJ/mol	165.79	NIST
Δ_fusH	9.20	kJ/mol	165.80	NIST
Δ_vapH	[30.79; 40.70]	kJ/mol	[246.50; 517.00]

Δ_vapH	40.70	kJ/mol	246.50	NIST
Δ_vapH	36.10	kJ/mol	311.00	NIST
Δ_vapH	34.40 ± 0.10	kJ/mol	313.00	NIST
Δ_vapH	34.30 ± 0.10	kJ/mol	313.00	NIST
Δ_vapH	33.40 ± 0.10	kJ/mol	328.00	NIST
Δ_vapH	33.20 ± 0.10	kJ/mol	333.00	NIST
Δ_vapH	34.80	kJ/mol	335.50	NIST
Δ_vapH	32.60 ± 0.10	kJ/mol	343.00	NIST
Δ_vapH	32.00 ± 0.10	kJ/mol	353.00	NIST
Δ_vapH	31.70 ± 0.10	kJ/mol	358.00	NIST
Δ_vapH	33.90	kJ/mol	358.50	NIST
Δ_vapH	31.00 ± 0.10	kJ/mol	368.00	NIST
Δ_vapH	31.00	kJ/mol	371.00	NIST
Δ_vapH	31.01	kJ/mol	372.40	KDB
Δ_vapH	30.79	kJ/mol	372.40	NIST
Δ_vapH	32.20	kJ/mol	394.00	NIST
Δ_vapH	31.50	kJ/mol	453.50	NIST
Δ_vapH	31.60	kJ/mol	473.00	NIST
Δ_vapH	31.40	kJ/mol	517.00	NIST
ν	[0.0000005; 0.0000007]	m²/s	[293.15; 323.15]

ν	0.0000007	m²/s	293.15	Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν	0.0000007	m²/s	298.15	Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν	0.0000007	m²/s	303.15	Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν	0.0000006	m²/s	313.15	Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν	0.0000005	m²/s	323.15	Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
P_vap	[3.05; 282.80]	kPa	[283.60; 413.15]

P_vap	3.05	kPa	283.60	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	3.99	kPa	288.40	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	5.18	kPa	293.40	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	6.63	kPa	298.30	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	6.62	kPa	298.40	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	8.33	kPa	303.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
P_vap	8.39	kPa	303.30	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	10.44	kPa	308.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
P_vap	10.53	kPa	308.20	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	12.97	kPa	313.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	12.95	kPa	313.15	Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
P_vap	12.95	kPa	313.15	Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
P_vap	13.01	kPa	313.15	Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
P_vap	12.96	kPa	313.15	Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
P_vap	12.97	kPa	313.15	Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
P_vap	12.97	kPa	313.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
P_vap	15.96	kPa	318.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	15.98	kPa	318.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
P_vap	19.54	kPa	323.00	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	19.54	kPa	323.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
P_vap	20.00	kPa	323.65	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
P_vap	23.81	kPa	328.00	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	28.66	kPa	332.80	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
P_vap	100.05	kPa	371.55	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	101.30	kPa	372.26	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
P_vap	101.30	kPa	372.33	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
P_vap	101.33	kPa	372.35	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
P_vap	103.49	kPa	373.10	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
P_vap	104.94	kPa	373.40	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	124.90	kPa	379.80	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	149.96	kPa	386.94	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	174.70	kPa	393.14	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	199.94	kPa	398.64	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	224.91	kPa	403.68	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	249.95	kPa	408.28	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	250.00	kPa	408.30	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	282.80	kPa	413.15	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
n₀	[1.37898; 1.39404]		[288.15; 318.15]

n₀	1.39404		288.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n₀	1.39404		288.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n₀	1.38894		293.15	Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
n₀	1.38921		298.10	Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
n₀	1.38900		298.15	A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
n₀	1.38902		298.15	Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
n₀	1.38890		298.15	Phase equilibria on four binary systems containing 3-methylthiophene
n₀	1.38890		298.15	Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
n₀	1.38800		298.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n₀	1.38898		298.15	KDB
n₀	1.38887		298.15	Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
n₀	1.38890		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n₀	1.38905		298.15	Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
n₀	1.38894		298.15	Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
n₀	1.38904		298.15	(Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
n₀	1.38901		298.15	Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
n₀	1.38887		298.15	Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
n₀	1.38887		298.15	Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
n₀	1.38905		298.15	Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
n₀	1.38898		298.15	Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
n₀	1.38917		298.15	Liquid liquid equilibria of lactam containing binary systems
n₀	1.38900		298.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n₀	1.38900		298.15	Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
n₀	1.38898		298.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n₀	1.38920		298.15	Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
n₀	1.38900		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
n₀	1.38894		298.15	Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
n₀	1.38900		298.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n₀	1.38910		298.20	Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
n₀	1.38520		303.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n₀	1.38395		308.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n₀	1.38398		308.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n₀	1.38395		308.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n₀	1.38240		308.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n₀	1.37898		318.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
ρ_l	[649.40; 704.10]	kg/m³	[278.15; 343.15]

ρ_l	704.10	kg/m³	278.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	700.05	kg/m³	283.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	695.98	kg/m³	288.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	692.00	kg/m³	293.00	KDB
ρ_l	691.88	kg/m³	293.00	Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρ_l	692.00	kg/m³	293.15	Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
ρ_l	691.89	kg/m³	293.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρ_l	691.91	kg/m³	293.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	691.84	kg/m³	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	691.83	kg/m³	293.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	692.05	kg/m³	293.15	Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
ρ_l	691.89	kg/m³	293.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	690.40	kg/m³	295.00	High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran + iso-octane) and (2-methyltetrahydrofuran + di-n-butyl ether): Experiments and PCP-SAFT modeling
ρ_l	687.82	kg/m³	298.15	Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) at 101.3 kPa
ρ_l	688.03	kg/m³	298.15	Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
ρ_l	687.62	kg/m³	298.15	Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
ρ_l	687.82	kg/m³	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	687.72	kg/m³	298.15	Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
ρ_l	687.77	kg/m³	298.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	687.70	kg/m³	298.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	688.18	kg/m³	298.15	Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
ρ_l	687.91	kg/m³	298.15	Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
ρ_l	687.77	kg/m³	298.15	Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
ρ_l	687.32	kg/m³	298.15	Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
ρ_l	687.75	kg/m³	298.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρ_l	687.32	kg/m³	298.15	Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
ρ_l	687.76	kg/m³	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρ_l	687.81	kg/m³	298.15	Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
ρ_l	687.74	kg/m³	298.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	687.72	kg/m³	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρ_l	683.64	kg/m³	303.00	Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρ_l	683.64	kg/m³	303.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	683.68	kg/m³	303.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	683.59	kg/m³	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	683.61	kg/m³	303.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρ_l	683.74	kg/m³	303.15	Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane
ρ_l	683.61	kg/m³	303.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	679.48	kg/m³	308.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	679.51	kg/m³	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	679.47	kg/m³	308.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	679.44	kg/m³	308.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρ_l	679.40	kg/m³	308.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	675.30	kg/m³	313.00	Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρ_l	675.28	kg/m³	313.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	675.32	kg/m³	313.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	675.23	kg/m³	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	675.29	kg/m³	313.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	675.25	kg/m³	313.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρ_l	675.23	kg/m³	313.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρ_l	671.07	kg/m³	318.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	670.98	kg/m³	318.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	671.05	kg/m³	318.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	671.09	kg/m³	318.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	666.84	kg/m³	323.00	Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρ_l	666.80	kg/m³	323.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	666.81	kg/m³	323.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	666.75	kg/m³	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	666.86	kg/m³	323.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρ_l	662.44	kg/m³	328.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	662.52	kg/m³	328.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	658.20	kg/m³	333.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρ_l	658.16	kg/m³	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	658.19	kg/m³	333.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	653.80	kg/m³	338.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	653.81	kg/m³	338.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	649.40	kg/m³	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρ_l	649.40	kg/m³	343.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρ_l	649.44	kg/m³	343.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
Δ_fusS	[54.70; 55.56]	J/mol×K	[165.30; 165.79]
Δ_fusS	54.70	J/mol×K	165.30	NIST
Δ_fusS	54.70	J/mol×K	165.30	NIST
Δ_fusS	55.56	J/mol×K	165.79	NIST
c_sound,fluid	[979.25; 1124.31]	m/s	[288.15; 323.15]

c_sound,fluid	1124.31	m/s	288.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
c_sound,fluid	1124.31	m/s	288.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1113.83	m/s	290.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1103.30	m/s	293.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1092.66	m/s	295.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1082.20	m/s	298.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1082.20	m/s	298.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
c_sound,fluid	1071.72	m/s	300.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1061.30	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1050.89	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1040.53	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1030.22	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1019.94	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	1009.71	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	999.53	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	989.37	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	979.25	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
c_sound,fluid	979.25	m/s	323.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
γ	[0.02; 0.02]	N/m	[288.15; 323.15]

γ	0.02	N/m	288.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	288.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	288.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	298.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	298.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	298.20	KDB
γ	0.02	N/m	303.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	308.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	308.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	313.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	318.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	323.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
λ	[0.09; 0.10]	W/m×K	[259.11; 328.14]

λ	0.10	W/m×K	259.11	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	259.32	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	259.52	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	277.52	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	277.74	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	277.93	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	295.67	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	295.90	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	296.10	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	313.79	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	314.02	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	314.22	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	327.69	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	327.93	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.09	W/m×K	328.14	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0005
293.15	1000.00	0.0005
293.15	5000.00	0.0005
293.15	10000.00	0.0006
293.15	20000.00	0.0006
293.15	30000.00	0.0007
293.15	40000.00	0.0008
293.15	50000.00	0.0009
293.15	60000.00	0.0010
293.15	70000.00	0.0010
293.15	80000.00	0.0011
293.15	100000.00	0.0013
293.15	120000.00	0.0015
293.15	140000.00	0.0017
298.15	100.00	0.0005
298.15	1000.00	0.0005
298.15	5000.00	0.0005
298.15	10000.00	0.0005
298.15	20000.00	0.0006
298.15	30000.00	0.0007
298.15	40000.00	0.0007
298.15	50000.00	0.0008
298.15	60000.00	0.0009
298.15	70000.00	0.0010
298.15	80000.00	0.0011
298.15	100000.00	0.0012
298.15	120000.00	0.0014
298.15	140000.00	0.0016
313.15	100.00	0.0004
313.15	1000.00	0.0004
313.15	5000.00	0.0004
313.15	10000.00	0.0005
313.15	20000.00	0.0005
313.15	30000.00	0.0006
313.15	40000.00	0.0006
313.15	50000.00	0.0007
313.15	60000.00	0.0008
313.15	70000.00	0.0008
313.15	80000.00	0.0009
313.15	100000.00	0.0010
313.15	120000.00	0.0012
313.15	140000.00	0.0014
323.15	100.00	0.0004
323.15	1000.00	0.0004
323.15	5000.00	0.0004
323.15	10000.00	0.0004
323.15	20000.00	0.0005
323.15	30000.00	0.0005
323.15	40000.00	0.0006
323.15	50000.00	0.0006
323.15	60000.00	0.0007
323.15	70000.00	0.0007
323.15	80000.00	0.0008
323.15	100000.00	0.0009
323.15	120000.00	0.0011
323.15	140000.00	0.0012
333.15	100.00	0.0003
333.15	1000.00	0.0003
333.15	5000.00	0.0004
333.15	10000.00	0.0004
333.15	20000.00	0.0004
333.15	30000.00	0.0005
333.15	40000.00	0.0005
333.15	50000.00	0.0006
333.15	60000.00	0.0006
333.15	70000.00	0.0007
333.15	80000.00	0.0007
333.15	100000.00	0.0008
333.15	120000.00	0.0010
333.15	140000.00	0.0011
348.15	100.00	0.0003
348.15	1000.00	0.0003
348.15	5000.00	0.0003
348.15	10000.00	0.0003
348.15	20000.00	0.0004
348.15	30000.00	0.0004
348.15	40000.00	0.0005
348.15	50000.00	0.0005
348.15	60000.00	0.0005
348.15	70000.00	0.0006
348.15	80000.00	0.0007
348.15	100000.00	0.0008
348.15	120000.00	0.0009
348.15	140000.00	0.0010
353.15	100.00	0.0003
353.15	1000.00	0.0003
353.15	5000.00	0.0003
353.15	10000.00	0.0003
353.15	20000.00	0.0004
353.15	30000.00	0.0004
353.15	40000.00	0.0004
353.15	50000.00	0.0005
353.15	60000.00	0.0005
353.15	70000.00	0.0006
353.15	80000.00	0.0006
353.15	100000.00	0.0007
353.15	120000.00	0.0008
353.15	140000.00	0.0009
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0005
Reference

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	101.33	1.3891
293.15	101.00	1.4211
303.15	101.00	1.416
313.15	101.00	1.4109
323.15	101.00	1.4055
293.15	101.00	1.3916
303.15	101.00	1.3866
313.15	101.00	1.3814
323.15	101.00	1.3763
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	687.32
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
294.06	100.00	1099.7
304.03	100.00	1058.5
313.81	100.00	1017.3
323.56	100.00	978.2
333.42	100.00	938.5
342.88	100.00	898.0
352.86	100.00	858.9
363.55	100.00	821.9
294.37	3000.00	1127.4
304.16	3000.00	1088.2
313.92	3000.00	1037.2
323.61	3000.00	999.1
333.48	3000.00	968.0
343.07	3000.00	927.9
352.89	3000.00	891.7
363.39	3000.00	852.2
373.04	3000.00	821.1
383.18	3000.00	783.2
393.83	3000.00	742.3
402.16	3000.00	716.5
412.57	3000.00	677.6
423.95	3000.00	636.8
434.51	3000.00	602.6
443.70	3000.00	569.7
452.94	3000.00	538.4
462.54	3000.00	502.1
472.45	3000.00	464.2
483.15	3000.00	423.5
493.12	3000.00	386.4
502.80	3000.00	350.1
512.41	3000.00	311.4
523.31	3000.00	264.5
294.65	6000.00	1147.6
304.23	6000.00	1109.6
313.96	6000.00	1065.2
323.65	6000.00	1027.4
333.50	6000.00	996.0
343.16	6000.00	954.8
352.94	6000.00	921.1
363.49	6000.00	883.5
373.27	6000.00	843.9
383.80	6000.00	813.8
394.00	6000.00	782.2
402.48	6000.00	750.9
412.84	6000.00	719.3
424.32	6000.00	678.1
434.94	6000.00	647.4
444.00	6000.00	619.6
453.22	6000.00	588.3
463.04	6000.00	558.9
472.86	6000.00	530.7
483.63	6000.00	496.7
493.56	6000.00	464.9
503.17	6000.00	435.4
513.04	6000.00	404.0
523.97	6000.00	371.4
294.84	10000.00	1176.1
304.27	10000.00	1136.9
313.82	10000.00	1100.1
323.67	10000.00	1060.4
333.46	10000.00	1028.0
343.22	10000.00	990.3
353.01	10000.00	961.7
363.54	10000.00	925.7
373.41	10000.00	888.2
384.11	10000.00	855.6
394.15	10000.00	825.8
402.64	10000.00	800.2
413.07	10000.00	766.7
424.49	10000.00	732.1
435.26	10000.00	701.0
444.22	10000.00	677.1
454.37	10000.00	648.8
463.43	10000.00	622.7
473.22	10000.00	596.3
484.05	10000.00	569.9
494.09	10000.00	542.2
503.79	10000.00	516.1
513.78	10000.00	491.8
524.59	10000.00	463.0
294.97	12000.00	1181.7
304.27	12000.00	1147.7
313.85	12000.00	1110.8
323.71	12000.00	1075.4
333.40	12000.00	1041.9
343.21	12000.00	1008.5
353.04	12000.00	975.5
363.58	12000.00	943.8
373.49	12000.00	908.6
384.26	12000.00	876.5
394.19	12000.00	848.1
402.78	12000.00	819.5
413.22	12000.00	791.3
424.59	12000.00	756.7
435.36	12000.00	726.5
444.36	12000.00	700.3
455.24	12000.00	671.1
463.72	12000.00	651.6
473.48	12000.00	627.7
484.30	12000.00	598.4
494.42	12000.00	576.5
504.09	12000.00	550.4
514.01	12000.00	526.6
524.70	12000.00	501.3
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.15	1104.6
100.00	303.15	1061.7
100.00	313.15	1019.1
100.00	323.15	977.9
100.00	333.15	935.8
100.00	343.15	897.3
100.00	353.15	858.2
100.00	363.15	817.2
100.00	373.15	780.4
10000.00	293.15	1178.5
10000.00	303.15	1139.3
10000.00	313.15	1100.9
10000.00	323.15	1063.5
10000.00	333.15	1026.6
10000.00	343.15	992.6
10000.00	353.15	958.0
10000.00	363.15	924.3
10000.00	373.15	891.0
20000.00	293.15	1244.6
20000.00	303.15	1208.6
20000.00	313.15	1173.0
20000.00	323.15	1138.8
20000.00	333.15	1105.2
20000.00	343.15	1071.6
20000.00	353.15	1041.7
20000.00	363.15	1011.1
20000.00	373.15	980.7
30000.00	293.15	1304.8
30000.00	303.15	1270.2
30000.00	313.15	1237.0
30000.00	323.15	1204.7
30000.00	333.15	1173.0
30000.00	343.15	1142.7
30000.00	353.15	1114.1
30000.00	363.15	1085.5
30000.00	373.15	1057.5
40000.00	293.15	1358.5
40000.00	303.15	1326.8
40000.00	313.15	1295.2
40000.00	323.15	1264.6
40000.00	333.15	1234.2
40000.00	343.15	1205.7
40000.00	353.15	1178.7
40000.00	363.15	1151.4
40000.00	373.15	1125.2
50000.00	293.15	1410.3
50000.00	303.15	1378.5
50000.00	313.15	1349.3
50000.00	323.15	1319.0
50000.00	333.15	1290.2
50000.00	343.15	1262.9
50000.00	353.15	1236.1
50000.00	363.15	1211.3
50000.00	373.15	1185.9
60000.00	293.15	1458.1
60000.00	303.15	1427.0
60000.00	313.15	1397.6
60000.00	323.15	1369.8
60000.00	333.15	1341.8
60000.00	343.15	1315.4
60000.00	353.15	1290.4
60000.00	363.15	1265.7
60000.00	373.15	1242.1
70000.00	293.15	1502.5
70000.00	303.15	1472.6
70000.00	313.15	1443.4
70000.00	323.15	1416.6
70000.00	333.15	1390.0
70000.00	343.15	1363.5
70000.00	353.15	1339.5
70000.00	363.15	1316.6
70000.00	373.15	1293.1
80000.00	293.15	1544.7
80000.00	303.15	1515.6
80000.00	313.15	1487.6
80000.00	323.15	1461.2
80000.00	333.15	1434.9
80000.00	343.15	1410.8
80000.00	353.15	1386.8
80000.00	363.15	1364.4
80000.00	373.15	1341.5
90000.00	293.15	1584.5
90000.00	303.15	1556.4
90000.00	313.15	1529.0
90000.00	323.15	1503.4
90000.00	333.15	1479.0
90000.00	343.15	1453.6
90000.00	353.15	1431.0
90000.00	363.15	1408.2
90000.00	373.15	1386.0
100000.00	293.15	1622.6
100000.00	303.15	1594.5
100000.00	313.15	1568.7
100000.00	323.15	1543.4
100000.00	333.15	1519.0
100000.00	343.15	1495.3
100000.00	353.15	1472.5
100000.00	363.15	1449.9
100000.00	373.15	1428.5
110000.00	293.15	1658.9
110000.00	303.15	1632.1
110000.00	313.15	1605.9
110000.00	323.15	1581.4
110000.00	333.15	1557.7
110000.00	343.15	1534.0
110000.00	353.15	1512.1
110000.00	363.15	1490.6
110000.00	373.15	1469.2
120000.00	293.15	1694.0
120000.00	303.15	1667.5
120000.00	313.15	1641.7
120000.00	323.15	1617.8
120000.00	333.15	1594.1
120000.00	343.15	1571.7
120000.00	353.15	1549.6
120000.00	363.15	1529.0
120000.00	373.15	1508.2
130000.00	293.15	1727.5
130000.00	303.15	1701.6
130000.00	313.15	1676.3
130000.00	323.15	1653.1
130000.00	333.15	1629.5
130000.00	343.15	1607.2
130000.00	353.15	1585.9
130000.00	363.15	1565.5
130000.00	373.15	1545.1
140000.00	293.15	1760.1
140000.00	303.15	1734.3
140000.00	313.15	1709.4
140000.00	323.15	1686.4
140000.00	333.15	1663.5
140000.00	343.15	1641.7
140000.00	353.15	1620.5
140000.00	363.15	1600.8
140000.00	373.15	1580.3
150000.00	293.15	1791.1
150000.00	303.15	1766.4
150000.00	313.15	1741.7
150000.00	323.15	1718.6
150000.00	333.15	1696.2
150000.00	343.15	1675.0
150000.00	353.15	1654.1
150000.00	363.15	1634.2
150000.00	373.15	1614.0
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
77.00	295.00	0.0960
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
254.60	100.00	0.1047
254.51	5000.00	0.1066
254.67	10100.00	0.1088
254.77	20000.00	0.1121
254.73	30000.00	0.1157
274.66	100.00	0.1004
274.63	5000.00	0.1021
274.61	10000.00	0.1041
274.61	20000.00	0.1080
274.57	30000.00	0.1114
295.33	100.00	0.0959
295.22	5000.00	0.0979
295.22	10100.00	0.1003
295.06	20100.00	0.1042
295.04	30100.00	0.1083
314.99	100.00	0.0907
314.85	5000.00	0.0930
314.87	10000.00	0.0953
314.93	20000.00	0.0996
314.91	29900.00	0.1038
334.53	100.00	0.0859
334.49	5100.00	0.0886
334.56	10000.00	0.0908
334.62	20000.00	0.0958
334.59	30000.00	0.0999
354.50	200.00	0.0817
354.78	5100.00	0.0843
354.83	10000.00	0.0868
354.73	20000.00	0.0915
354.80	30000.00	0.0960
374.63	400.00	0.0784
374.61	5000.00	0.0807
374.18	10000.00	0.0830
374.21	19900.00	0.0875
374.25	29900.00	0.0925
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.67]	kPa	[268.57; 398.53]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.40806e+01
Coefficient B			-3.12864e+03
Coefficient C			-4.17450e+01
Temperature range, min.			268.57
Temperature range, max.			398.53

P_vap	1.33	kPa	268.57	Calculated Property
P_vap	3.04	kPa	283.01	Calculated Property
P_vap	6.33	kPa	297.45	Calculated Property
P_vap	12.17	kPa	311.89	Calculated Property
P_vap	21.91	kPa	326.33	Calculated Property
P_vap	37.25	kPa	340.77	Calculated Property
P_vap	60.32	kPa	355.21	Calculated Property
P_vap	93.62	kPa	369.65	Calculated Property
P_vap	140.01	kPa	384.09	Calculated Property
P_vap	202.67	kPa	398.53	Calculated Property
P_vap	[1.48e-05; 2584.81]	kPa	[165.78; 543.96]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			8.67458e+01
Coefficient B			-7.04177e+03
Coefficient C			-1.08858e+01
Coefficient D			8.87277e-06
Temperature range, min.			165.78
Temperature range, max.			543.96

P_vap	1.48e-05	kPa	165.78	Calculated Property
P_vap	7.82e-03	kPa	207.80	Calculated Property
P_vap	0.37	kPa	249.82	Calculated Property
P_vap	4.87	kPa	291.84	Calculated Property
P_vap	29.62	kPa	333.86	Calculated Property
P_vap	112.21	kPa	375.88	Calculated Property
P_vap	313.08	kPa	417.90	Calculated Property
P_vap	713.56	kPa	459.92	Calculated Property
P_vap	1420.70	kPa	501.94	Calculated Property
P_vap	2584.81	kPa	543.96	Calculated Property

Similar Compounds

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Mixtures

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Sources

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Chemical Properties of Pentane, 2,2,4-trimethyl- (CAS 540-84-1)

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