Chemical Properties of Benzene, 1,2,4-trimethyl- (CAS 95-63-6)

InChI

InChI=1S/C9H12/c1-7-4-5-8(2)9(3)6-7/h4-6H,1-3H3

InChI Key

GWHJZXXIDMPWGX-UHFFFAOYSA-N

Formula

C9H12

SMILES

Cc1ccc(C)c(C)c1

Molecular Weight¹

120.19

CAS

95-63-6

Other Names

• 1,2,4-Trimethylbenzene
• 1,2,4-trimethylbenzene (pseudocumene)
• 1,2,5-Trimethylbenzene
• 1,3,4-Trimethylbenzene
• AS-TRIMETHYBENZENE
• Asymmetrical trimethylbenzene
• Benzene, 1,2,5-trimethyl-
• NSC 65600
• PSEUDOCUMENE
• Pseudocumol
• Psi-cumene
• as-Trimethylbenzene
• «psi»-Cumene
• «psi»-Cumene

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• 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_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3760		KDB
ΔcH°liquid	[-5194.80; -5190.60]	kJ/mol
ΔcH°liquid	-5194.80 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-5190.60	kJ/mol	NIST
Cp,liquid	213.02	J/mol×K	Thermod...
ΔfG°	117.00	kJ/mol	KDB
Δc,grossH	5194.77	kJ/mol	KDB
Δc,netH	4930.677	kJ/mol	KDB
ΔfH°gas	[-13.94; -13.90]	kJ/mol
ΔfH°gas	-13.94	kJ/mol	KDB
ΔfH°gas	-13.90 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-61.90 ± 1.10	kJ/mol	NIST
ΔfusH°	12.33	kJ/mol	Joback Calculated Property
ΔvapH°	[39.30; 48.00]	kJ/mol
ΔvapH°	47.94	kJ/mol	NIST
ΔvapH°	48.00	kJ/mol	NIST
ΔvapH°	47.20	kJ/mol	NIST
ΔvapH°	47.90	kJ/mol	NIST
ΔvapH°	Outlier 39.30	kJ/mol	NIST
ΔvapH°	47.90	kJ/mol	NIST
ΔvapH°	47.93	kJ/mol	NIST
ΔvapH°	48.00	kJ/mol	NIST
IE	[8.27; 8.50]	eV
IE	8.27 ± 0.01	eV	NIST
IE	8.27	eV	NIST
IE	8.27 ± 0.01	eV	NIST
IE	8.27	eV	NIST
IE	8.50 ± 0.03	eV	NIST
log10WS	[-3.31; -3.31]
log10WS	-3.31		Aq. Sol...
log10WS	-3.31		Estimat...
logPoct/wat	2.612		Crippen Calculated Property
McVol	113.910	ml/mol	McGowan Calculated Property
Pc	[1925.18; 3382.60]	kPa
Pc	3232.00	kPa	KDB
Pc	3277.10 ± 0.32	kPa	NIST
Pc	3269.40 ± 0.32	kPa	NIST
Pc	3269.50 ± 0.32	kPa	NIST
Pc	3382.60 ± 0.33	kPa	NIST
Pc	3232.00 ± 6.00	kPa	NIST
Pc	Outlier 1925.18 ± 151.99	kPa	NIST
Pc	3260.00 ± 5.88	kPa	NIST
Inp	[173.80; 1026.00]
Inp	1005.50		NIST
Inp	1012.30		NIST
Inp	969.90		NIST
Inp	975.30		NIST
Inp	976.05		NIST
Inp	990.10		NIST
Inp	1006.00		NIST
Inp	1006.00		NIST
Inp	1006.00		NIST
Inp	995.00		NIST
Inp	1004.20		NIST
Inp	1013.40		NIST
Inp	986.00		NIST
Inp	975.00		NIST
Inp	975.00		NIST
Inp	986.00		NIST
Inp	986.00		NIST
Inp	987.30		NIST
Inp	986.90		NIST
Inp	987.90		NIST
Inp	988.00		NIST
Inp	976.20		NIST
Inp	980.50		NIST
Inp	991.90		NIST
Inp	996.60		NIST
Inp	987.00		NIST
Inp	993.00		NIST
Inp	1017.00		NIST
Inp	987.00		NIST
Inp	987.00		NIST
Inp	987.00		NIST
Inp	987.00		NIST
Inp	987.00		NIST
Inp	988.00		NIST
Inp	986.00		NIST
Inp	988.00		NIST
Inp	986.00		NIST
Inp	989.00		NIST
Inp	983.00		NIST
Inp	986.00		NIST
Inp	984.00		NIST
Inp	975.60		NIST
Inp	976.00		NIST
Inp	977.50		NIST
Inp	1000.00		NIST
Inp	984.00		NIST
Inp	988.00		NIST
Inp	994.00		NIST
Inp	1001.00		NIST
Inp	982.00		NIST
Inp	985.30		NIST
Inp	988.40		NIST
Inp	994.10		NIST
Inp	1001.30		NIST
Inp	980.00		NIST
Inp	990.00		NIST
Inp	982.40		NIST
Inp	982.50		NIST
Inp	982.80		NIST
Inp	982.20		NIST
Inp	982.80		NIST
Inp	982.80		NIST
Inp	985.30		NIST
Inp	987.00		NIST
Inp	979.70		NIST
Inp	988.00		NIST
Inp	974.90		NIST
Inp	988.20		NIST
Inp	991.00		NIST
Inp	981.00		NIST
Inp	990.40		NIST
Inp	982.20		NIST
Inp	990.00		NIST
Inp	994.00		NIST
Inp	976.00		NIST
Inp	993.90		NIST
Inp	984.00		NIST
Inp	977.00		NIST
Inp	1016.00		NIST
Inp	983.20		NIST
Inp	983.00		NIST
Inp	978.40		NIST
Inp	978.40		NIST
Inp	999.00		NIST
Inp	981.00		NIST
Inp	988.00		NIST
Inp	1023.00		NIST
Inp	984.70		NIST
Inp	987.50		NIST
Inp	991.10		NIST
Inp	992.80		NIST
Inp	1000.00		NIST
Inp	1004.00		NIST
Inp	991.00		NIST
Inp	979.30		NIST
Inp	976.00		NIST
Inp	987.50		NIST
Inp	991.10		NIST
Inp	992.80		NIST
Inp	978.00		NIST
Inp	978.78		NIST
Inp	980.80		NIST
Inp	979.00		NIST
Inp	988.00		NIST
Inp	978.53		NIST
Inp	979.40		NIST
Inp	973.20		NIST
Inp	973.60		NIST
Inp	980.60		NIST
Inp	972.82		NIST
Inp	976.75		NIST
Inp	978.96		NIST
Inp	989.41		NIST
Inp	993.40		NIST
Inp	996.08		NIST
Inp	977.00		NIST
Inp	985.00		NIST
Inp	1001.97		NIST
Inp	982.00		NIST
Inp	1012.00		NIST
Inp	1001.00		NIST
Inp	980.00		NIST
Inp	983.00		NIST
Inp	988.00		NIST
Inp	989.00		NIST
Inp	994.00		NIST
Inp	994.00		NIST
Inp	978.00		NIST
Inp	992.00		NIST
Inp	990.00		NIST
Inp	979.00		NIST
Inp	993.00		NIST
Inp	994.00		NIST
Inp	986.00		NIST
Inp	989.00		NIST
Inp	983.00		NIST
Inp	994.00		NIST
Inp	995.00		NIST
Inp	1025.00		NIST
Inp	1012.00		NIST
Inp	986.00		NIST
Inp	1026.00		NIST
Inp	997.00		NIST
Inp	1021.00		NIST
Inp	1021.00		NIST
Inp	966.00		NIST
Inp	1000.00		NIST
Inp	974.00		NIST
Inp	985.00		NIST
Inp	984.00		NIST
Inp	984.00		NIST
Inp	990.00		NIST
Inp	980.24		NIST
Inp	981.00		NIST
Inp	976.00		NIST
Inp	997.50		NIST
Inp	956.00		NIST
Inp	957.00		NIST
Inp	987.00		NIST
Inp	971.00		NIST
Inp	975.00		NIST
Inp	976.00		NIST
Inp	990.00		NIST
Inp	956.00		NIST
Inp	984.00		NIST
Inp	979.00		NIST
Inp	979.00		NIST
Inp	969.00		NIST
Inp	994.00		NIST
Inp	1026.00		NIST
Inp	1020.00		NIST
Inp	1021.00		NIST
Inp	968.00		NIST
Inp	985.00		NIST
Inp	1023.00		NIST
Inp	991.00		NIST
Inp	961.00		NIST
Inp	989.00		NIST
Inp	978.00		NIST
Inp	990.00		NIST
Inp	988.00		NIST
Inp	976.00		NIST
Inp	984.00		NIST
Inp	984.00		NIST
Inp	973.00		NIST
Inp	976.00		NIST
Inp	984.00		NIST
Inp	1012.00		NIST
Inp	978.00		NIST
Inp	988.00		NIST
Inp	978.00		NIST
Inp	988.00		NIST
Inp	978.00		NIST
Inp	956.00		NIST
Inp	978.00		NIST
Inp	986.30		NIST
Inp	971.00		NIST
Inp	978.00		NIST
Inp	1001.00		NIST
Inp	975.00		NIST
Inp	977.00		NIST
Inp	1000.00		NIST
Inp	992.00		NIST
Inp	Outlier 173.80		NIST
Inp	983.20		NIST
I	[1247.00; 1333.00]
I	1312.40		NIST
I	Outlier 1326.70		NIST
I	Outlier 1247.00		NIST
I	1249.00		NIST
I	1277.60		NIST
I	1272.20		NIST
I	1253.10		NIST
I	1300.00		NIST
I	1310.00		NIST
I	Outlier 1319.00		NIST
I	1291.00		NIST
I	1285.00		NIST
I	1275.00		NIST
I	1257.00		NIST
I	1292.00		NIST
I	1252.00		NIST
I	1308.10		NIST
I	1285.00		NIST
I	1285.00		NIST
I	1293.00		NIST
I	1267.00		NIST
I	1275.00		NIST
I	1291.00		NIST
I	1293.00		NIST
I	1285.00		NIST
I	1285.00		NIST
I	1278.00		NIST
I	1278.00		NIST
I	1280.00		NIST
I	1281.00		NIST
I	1285.00		NIST
I	1287.00		NIST
I	1289.00		NIST
I	1285.00		NIST
I	1286.00		NIST
I	1283.00		NIST
I	1280.00		NIST
I	1280.00		NIST
I	1253.00		NIST
I	1275.00		NIST
I	1274.00		NIST
I	1289.00		NIST
I	1276.00		NIST
I	1276.00		NIST
I	1279.00		NIST
I	1290.00		NIST
I	Outlier 1333.00		NIST
I	1287.00		NIST
I	1275.00		NIST
I	1267.00		NIST
I	1294.00		NIST
I	1277.00		NIST
I	1278.00		NIST
I	1294.00		NIST
I	1294.00		NIST
I	1253.00		NIST
I	1288.00		NIST
I	1311.00		NIST
I	1278.00		NIST
I	1311.00		NIST
I	1277.00		NIST
I	1260.00		NIST
I	1283.00		NIST
S°gas	395.76 ± 0.63	J/mol×K	NIST
S°liquid	[283.30; 283.38]	J/mol×K
S°liquid	283.38	J/mol×K	NIST
S°liquid	283.30	J/mol×K	NIST
Tboil	[439.00; 443.35]	K
Tboil	442.53	K	KDB
Tboil	442.45	K	Isobari...
Tboil	441.20	K	NIST
Tboil	442.50	K	NIST
Tboil	442.50 ± 0.20	K	NIST
Tboil	442.49 ± 0.15	K	NIST
Tboil	442.49 ± 0.20	K	NIST
Tboil	442.00 ± 3.00	K	NIST
Tboil	Outlier 439.00 ± 2.00	K	NIST
Tboil	442.50 ± 0.03	K	NIST
Tboil	442.50 ± 0.15	K	NIST
Tboil	442.35 ± 0.30	K	NIST
Tboil	442.49 ± 0.15	K	NIST
Tboil	442.50 ± 0.20	K	NIST
Tboil	442.50 ± 0.20	K	NIST
Tboil	442.50 ± 0.20	K	NIST
Tboil	442.49 ± 0.20	K	NIST
Tboil	442.60 ± 0.40	K	NIST
Tboil	442.65 ± 0.25	K	NIST
Tboil	442.00 ± 2.00	K	NIST
Tboil	442.70 ± 0.60	K	NIST
Tboil	442.50 ± 0.25	K	NIST
Tboil	442.50 ± 0.20	K	NIST
Tboil	442.55 ± 0.30	K	NIST
Tboil	442.55 ± 0.30	K	NIST
Tboil	441.35 ± 0.25	K	NIST
Tboil	442.00 ± 2.00	K	NIST
Tboil	442.90 ± 5.00	K	NIST
Tboil	442.33 ± 0.30	K	NIST
Tboil	442.30 ± 0.60	K	NIST
Tboil	442.30 ± 0.50	K	NIST
Tboil	443.35 ± 0.40	K	NIST
Tboil	442.10 ± 1.00	K	NIST
Tboil	442.42 ± 0.30	K	NIST
Tboil	441.40 ± 0.50	K	NIST
Tboil	442.90 ± 0.70	K	NIST
Tc	649.10	K	KDB
Tfus	[212.15; 229.37]	K
Tfus	229.30	K	KDB
Tfus	229.25	K	Aq. Sol...
Tfus	221.00 ± 4.00	K	NIST
Tfus	229.00 ± 0.20	K	NIST
Tfus	228.85 ± 0.20	K	NIST
Tfus	229.37 ± 0.20	K	NIST
Tfus	229.05 ± 0.40	K	NIST
Tfus	223.85 ± 0.40	K	NIST
Tfus	224.18 ± 0.20	K	NIST
Tfus	229.23 ± 0.10	K	NIST
Tfus	229.24 ± 0.08	K	NIST
Tfus	229.35 ± 0.07	K	NIST
Tfus	224.15 ± 0.07	K	NIST
Tfus	228.15 ± 2.00	K	NIST
Tfus	228.70 ± 0.60	K	NIST
Tfus	228.15 ± 0.20	K	NIST
Tfus	Outlier 212.15 ± 0.50	K	NIST
Ttriple	[228.60; 229.33]	K
Ttriple	229.33 ± 0.03	K	NIST
Ttriple	228.60 ± 0.30	K	NIST
Vc	0.435	m3/kmol	KDB
Zc	0.2605030		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[216.81; 285.90]	J/mol×K	[441.96; 651.95]
Cp,gas	216.81	J/mol×K	441.96	Joback Calculated Property
Cp,gas	229.86	J/mol×K	476.96	Joback Calculated Property
Cp,gas	242.27	J/mol×K	511.96	Joback Calculated Property
Cp,gas	254.06	J/mol×K	546.96	Joback Calculated Property
Cp,gas	265.25	J/mol×K	581.96	Joback Calculated Property
Cp,gas	275.86	J/mol×K	616.95	Joback Calculated Property
Cp,gas	285.90	J/mol×K	651.95	Joback Calculated Property
Cp,liquid	[210.41; 214.97]	J/mol×K	[295.99; 299.80]
Cp,liquid	212.10	J/mol×K	295.99	NIST
Cp,liquid	212.10	J/mol×K	297.30	NIST
Cp,liquid	213.00	J/mol×K	298.00	NIST
Cp,liquid	213.11	J/mol×K	298.15	NIST
Cp,liquid	214.97	J/mol×K	298.15	NIST
Cp,liquid	210.41	J/mol×K	299.80	NIST
η	[0.0002083; 0.0015760]	Pa×s	[242.65; 441.96]
η	0.0015760	Pa×s	242.65	Joback Calculated Property
η	0.0009182	Pa×s	275.87	Joback Calculated Property
η	0.0006008	Pa×s	309.09	Joback Calculated Property
η	0.0004268	Pa×s	342.31	Joback Calculated Property
η	0.0003221	Pa×s	375.52	Joback Calculated Property
η	0.0002545	Pa×s	408.74	Joback Calculated Property
η	0.0002083	Pa×s	441.96	Joback Calculated Property
ΔfusH	[12.65; 13.19]	kJ/mol	[228.60; 229.30]
ΔfusH	12.65	kJ/mol	228.60	NIST
ΔfusH	13.19	kJ/mol	229.30	NIST
ΔvapH	[39.25; 46.50]	kJ/mol	[262.00; 442.30]
ΔvapH	46.50	kJ/mol	262.00	NIST
ΔvapH	44.10	kJ/mol	403.50	NIST
ΔvapH	39.25	kJ/mol	442.30	KDB
Pvap	[0.73; 101.40]	kPa	[313.15; 442.22]
Pvap	0.73	kPa	313.15	Vapor-l...
Pvap	16.90	kPa	383.15	Phase e...
Pvap	20.10	kPa	387.74	Phase e...
Pvap	30.30	kPa	400.11	Phase e...
Pvap	39.80	kPa	408.87	Phase e...
Pvap	50.30	kPa	416.75	Phase e...
Pvap	60.00	kPa	422.84	Phase e...
Pvap	70.30	kPa	428.53	Phase e...
Pvap	80.30	kPa	433.42	Phase e...
Pvap	90.40	kPa	437.83	Phase e...
Pvap	101.40	kPa	442.22	Phase e...
n0	[1.50237; 1.50470]		[293.15; 298.15]
n0	1.50470		293.15	Isobari...
n0	1.50237		298.15	KDB
ρl	[871.64; 880.00]	kg/m3	[289.00; 298.15]
ρl	880.00	kg/m3	289.00	KDB
ρl	875.78	kg/m3	293.15	Isobari...
ρl	871.64	kg/m3	298.15	Excess ...
ρl	871.64	kg/m3	298.15	Excess ...
ΔfusS	55.30	J/mol×K	228.60	NIST
γ	[0.03; 0.03]	N/m	[293.20; 313.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Excess ...
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	298.15	Excess ...
γ	0.03	N/m	298.15	Excess ...
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	303.15	Densiti...
γ	0.03	N/m	308.15	Excess ...
γ	0.03	N/m	308.15	Excess ...
γ	0.03	N/m	308.15	Densiti...
γ	0.03	N/m	313.15	Densiti...
γ	0.03	N/m	313.15	Excess ...
γ	0.03	N/m	313.15	Excess ...
γ	0.03	N/m	313.15	Excess ...
γ	0.03	N/m	313.15	Densiti...
γ	0.03	N/m	313.15	Excess ...
λ	[0.12; 0.13]	W/m×K	[257.58; 331.09]
λ	0.13	W/m×K	257.58	Thermal...
λ	0.13	W/m×K	257.79	Thermal...
λ	0.13	W/m×K	257.93	Thermal...
λ	0.13	W/m×K	276.33	Thermal...
λ	0.13	W/m×K	276.54	Thermal...
λ	0.13	W/m×K	276.69	Thermal...
λ	0.13	W/m×K	283.32	Thermal...
λ	0.13	W/m×K	283.54	Thermal...
λ	0.13	W/m×K	283.68	Thermal...
λ	0.13	W/m×K	295.54	Thermal...
λ	0.13	W/m×K	295.76	Thermal...
λ	0.13	W/m×K	295.91	Thermal...
λ	0.12	W/m×K	312.75	Thermal...
λ	0.12	W/m×K	312.98	Thermal...
λ	0.12	W/m×K	313.13	Thermal...
λ	0.12	W/m×K	330.69	Thermal...
λ	0.12	W/m×K	330.93	Thermal...
λ	0.12	W/m×K	331.09	Thermal...

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0009
293.15	1000.00	0.0009
293.15	5000.00	0.0009
293.15	10000.00	0.0010
293.15	20000.00	0.0011
293.15	30000.00	0.0011
293.15	40000.00	0.0012
293.15	50000.00	0.0013
293.15	60000.00	0.0014
293.15	70000.00	0.0016
293.15	80000.00	0.0017
293.15	100000.00	0.0020
293.15	120000.00	0.0023
293.15	140000.00	0.0027
313.15	100.00	0.0007
313.15	1000.00	0.0007
313.15	5000.00	0.0007
313.15	10000.00	0.0008
313.15	20000.00	0.0008
313.15	30000.00	0.0009
313.15	40000.00	0.0010
313.15	50000.00	0.0010
313.15	60000.00	0.0011
313.15	70000.00	0.0012
313.15	80000.00	0.0012
313.15	100000.00	0.0014
313.15	120000.00	0.0016
313.15	140000.00	0.0018
333.15	100.00	0.0006
333.15	1000.00	0.0006
333.15	5000.00	0.0006
333.15	10000.00	0.0006
333.15	20000.00	0.0006
333.15	30000.00	0.0007
333.15	40000.00	0.0007
333.15	50000.00	0.0008
333.15	60000.00	0.0008
333.15	70000.00	0.0009
333.15	80000.00	0.0010
333.15	100000.00	0.0011
333.15	120000.00	0.0012
333.15	140000.00	0.0013
353.15	100.00	0.0005
353.15	1000.00	0.0005
353.15	5000.00	0.0005
353.15	10000.00	0.0005
353.15	20000.00	0.0005
353.15	30000.00	0.0006
353.15	40000.00	0.0006
353.15	50000.00	0.0006
353.15	60000.00	0.0007
353.15	70000.00	0.0007
353.15	80000.00	0.0008
353.15	100000.00	0.0009
353.15	120000.00	0.0010
353.15	140000.00	0.0011
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
273.15	100.00	891.7
273.15	1000.00	892.3
273.15	2000.00	892.9
273.15	5000.00	894.6
273.15	10000.00	897.4
273.15	15000.00	900.2
273.15	20000.00	902.8
273.15	30000.00	908.0
273.15	40000.00	912.9
273.15	50000.00	917.5
273.15	60000.00	921.9
273.15	70000.00	926.2
273.15	80000.00	930.3
273.15	90000.00	934.2
273.15	100000.00	938.0
273.15	110000.00	941.7
273.15	120000.00	945.2
273.15	130000.00	948.6
273.15	140000.00	952.0
283.15	100.00	883.3
283.15	1000.00	883.9
283.15	2000.00	884.5
283.15	5000.00	886.3
283.15	10000.00	889.3
283.15	15000.00	892.2
283.15	20000.00	895.0
283.15	30000.00	900.3
283.15	40000.00	905.4
283.15	50000.00	910.2
283.15	60000.00	914.8
283.15	70000.00	919.3
283.15	80000.00	923.5
283.15	90000.00	927.5
283.15	100000.00	931.4
283.15	110000.00	935.2
283.15	120000.00	938.9
283.15	130000.00	942.4
283.15	140000.00	945.8
293.15	100.00	875.1
293.15	1000.00	875.7
293.15	2000.00	876.3
293.15	5000.00	878.2
293.15	10000.00	881.4
293.15	15000.00	884.4
293.15	20000.00	887.3
293.15	30000.00	892.9
293.15	40000.00	898.2
293.15	50000.00	903.2
293.15	60000.00	908.0
293.15	70000.00	912.6
293.15	80000.00	916.9
293.15	90000.00	921.1
293.15	100000.00	925.1
293.15	110000.00	929.0
293.15	120000.00	932.8
293.15	130000.00	936.4
293.15	140000.00	939.9
303.15	100.00	867.0
303.15	1000.00	867.6
303.15	2000.00	868.3
303.15	5000.00	870.3
303.15	10000.00	873.6
303.15	15000.00	876.8
303.15	20000.00	879.8
303.15	30000.00	885.7
303.15	40000.00	891.2
303.15	50000.00	896.4
303.15	60000.00	901.4
303.15	70000.00	906.1
303.15	80000.00	910.6
303.15	90000.00	914.9
303.15	100000.00	919.1
303.15	110000.00	923.1
303.15	120000.00	927.0
303.15	130000.00	930.7
303.15	140000.00	934.3
313.15	100.00	859.0
313.15	1000.00	859.7
313.15	2000.00	860.4
313.15	5000.00	862.6
313.15	10000.00	866.0
313.15	15000.00	869.3
313.15	20000.00	872.6
313.15	30000.00	878.7
313.15	40000.00	884.5
313.15	50000.00	889.9
313.15	60000.00	895.0
313.15	70000.00	899.9
313.15	80000.00	904.6
313.15	90000.00	909.0
313.15	100000.00	913.3
313.15	110000.00	917.4
313.15	120000.00	921.4
313.15	130000.00	925.2
313.15	140000.00	928.9
323.15	100.00	851.3
323.15	1000.00	852.0
323.15	2000.00	852.7
323.15	5000.00	855.0
323.15	10000.00	858.6
323.15	15000.00	862.1
323.15	20000.00	865.5
323.15	30000.00	871.9
323.15	40000.00	877.9
323.15	50000.00	883.5
323.15	60000.00	888.9
323.15	70000.00	894.0
323.15	80000.00	898.8
323.15	90000.00	903.4
323.15	100000.00	907.8
323.15	110000.00	912.0
323.15	120000.00	916.1
323.15	130000.00	920.0
323.15	140000.00	923.8
333.15	100.00	843.6
333.15	1000.00	844.4
333.15	2000.00	845.2
333.15	5000.00	847.6
333.15	10000.00	851.4
333.15	15000.00	855.1
333.15	20000.00	858.6
333.15	30000.00	865.3
333.15	40000.00	871.6
333.15	50000.00	877.4
333.15	60000.00	883.0
333.15	70000.00	888.2
333.15	80000.00	893.2
333.15	90000.00	898.0
333.15	100000.00	902.5
333.15	110000.00	906.9
333.15	120000.00	911.1
333.15	130000.00	915.1
333.15	140000.00	919.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[323.10; 471.79]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.47784e+01
Coefficient B			-4.06027e+03
Coefficient C			-4.29020e+01
Temperature range, min.			323.10
Temperature range, max.			471.79
Pvap	1.33	kPa	323.10	Calculated Property
Pvap	2.99	kPa	339.62	Calculated Property
Pvap	6.15	kPa	356.14	Calculated Property
Pvap	11.77	kPa	372.66	Calculated Property
Pvap	21.18	kPa	389.18	Calculated Property
Pvap	36.13	kPa	405.71	Calculated Property
Pvap	58.82	kPa	422.23	Calculated Property
Pvap	91.95	kPa	438.75	Calculated Property
Pvap	138.68	kPa	455.27	Calculated Property
Pvap	202.65	kPa	471.79	Calculated Property
Pvap	[8.99e-04; 3155.22]	kPa	[229.38; 649.13]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.15931e+01
Coefficient B			-7.42775e+03
Coefficient C			-6.69353e+00
Coefficient D			2.96938e-06
Temperature range, min.			229.38
Temperature range, max.			649.13
Pvap	8.99e-04	kPa	229.38	Calculated Property
Pvap	0.07	kPa	276.02	Calculated Property
Pvap	1.24	kPa	322.66	Calculated Property
Pvap	10.13	kPa	369.30	Calculated Property
Pvap	48.58	kPa	415.94	Calculated Property
Pvap	163.06	kPa	462.57	Calculated Property
Pvap	426.85	kPa	509.21	Calculated Property
Pvap	935.65	kPa	555.85	Calculated Property
Pvap	1802.22	kPa	602.49	Calculated Property
Pvap	3155.22	kPa	649.13	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,2,4-trimethyl-.

Mixtures

• Thiophene, 3-methyl- + Benzene, 1,2,4-trimethyl-
• 1-Pentanol + Benzene, 1,2,4-trimethyl-
• 2-Pentanol + Benzene, 1,2,4-trimethyl-
• n-Propyl acetate + Benzene, 1,2,4-trimethyl-
• Acetic acid, butyl ester + Benzene, 1,2,4-trimethyl-
• Benzonitrile + Benzene, 1,2,4-trimethyl-
• Benzene, 1,2,4-trimethyl- + N-Formylmorpholine
• Benzene, 1-ethyl-3-methyl- + Benzene, 1,2,4-trimethyl-
• Benzene, 1-ethyl-4-methyl- + Benzene, 1,2,4-trimethyl-
• 1-Butanol + Benzene, 1,2,4-trimethyl-
• Benzene, 1,2,4-trimethyl- + Tetrahydrofuran
• Benzene, 1,2,4-trimethyl- + Carbon Tetrachloride
• Dimethyl Sulfoxide + Benzene, 1,2,4-trimethyl-
• 1-Propanol, 2-methyl- + Benzene, 1,2,4-trimethyl-
• 2-Propanol, 2-methyl- + Benzene, 1,2,4-trimethyl-
• Ethanol, 2-methoxy- + Benzene, 1,2,4-trimethyl-
• Ethane, 1,2-dimethoxy- + Benzene, 1,2,4-trimethyl-
• Carbonic acid, dimethyl ester + Benzene, 1,2,4-trimethyl-
• Diethyl carbonate + Benzene, 1,2,4-trimethyl-
• Benzene, 1,2,4-trimethyl- + Ethane, 1,1-diethoxy-

Find more mixtures with Benzene, 1,2,4-trimethyl-.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
• Liquid-liquid equilibria for ternary systems water + acetic acid + 1,2,4-trimethylbenzene and water + acetic acid + 1,3,5- trimethylbenzene at (303.2 - 343.2) K
• Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
• Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
• Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
• Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
• Isobaric VLE data for 1-methyl-3-ethylbenzene or 1-methyl-4-ethylbenzene + 1,2,4-trimethylbenzene at 20 kPa
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels
• Thermophysical properties of 1,2,4-trimethylbenzene in admixtures with 1-butanol or 2-butanol at high pressures
• Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
• Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
• Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
• Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
• Excess Molar Volumes and Surface Tensions of 1,2,4- Trimethylbenzene and 1,3,5- Trimethylbenzene with 1,1-Diethoxyethane and 2,2-Dimethoxypropane at (298.15, 308.15, and 313.15) K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Isobaric Vapor Liquid Equilibrium Data for the System of 1-Methyl-2-Ethylbenzene + 1,2,4-Trimethylbenzene at 10 kPa
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• 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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