Chemical Properties of Styrene (CAS 100-42-5)

InChI

InChI=1S/C8H8/c1-2-8-6-4-3-5-7-8/h2-7H,1H2

InChI Key

PPBRXRYQALVLMV-UHFFFAOYSA-N

Formula

C8H8

SMILES

C=Cc1ccccc1

Molecular Weight¹

104.15

CAS

100-42-5

Other Names

• Annamene
• Benzene, vinyl-
• Bulstren K-525-19
• Cinnamene
• Cinnamenol
• Cinnaminol
• Cinnamol
• Ethylene, phenyl-
• NCI-C02200
• NSC 62785
• Phenethylene
• Stirolo
• Styreen
• Styren
• Styrene monomer
• Styrol
• Styrol (German)
• Styrole
• Styrolene
• Styropol SO
• Vinylbenzen
• Vinylbenzene (styrene)
• Vinylbenzol
• benzene, ethenyl-
• ethenylbenzene
• ethenylbenzene (styrene)
• phenylethene
• phenylethylene
• vinylbenzene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : 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_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2570; 0.3007]
ω	0.3007		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2572		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2971		ChemSep v8.3 pure component data Compiled value
ω	0.2570		KDB
PAff	839.50	kJ/mol	NIST
Tig	763.15	K	KDB
BasG	809.20	kJ/mol	NIST
ΔcH°liquid	[-4438.35; -4336.70]	kJ/mol
ΔcH°liquid	-4395.63 ± 0.59	kJ/mol	NIST
ΔcH°liquid	-4394.87 ± 0.84	kJ/mol	NIST
ΔcH°liquid	-4438.35 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-4379.80 ± 6.30	kJ/mol	NIST
ΔcH°liquid	-4399.50	kJ/mol	NIST
ΔcH°liquid	-4374.40	kJ/mol	NIST
ΔcH°liquid	-4379.00	kJ/mol	NIST
ΔcH°liquid	-4431.30	kJ/mol	NIST
ΔcH°liquid	-4336.70	kJ/mol	NIST
μ	[0.10; 0.13]	debye
μ	0.13	debye	ChemSep v8.3 pure component data Compiled value
μ	0.10	debye	KDB
LFL	1.10	% in Air	KDB
UFL	6.10	% in Air	KDB
Tflash,cc	307.04	K	KDB
Tflash,oc	304.26	K	KDB
ΔfG°	[213.90; 213.90]	kJ/mol
ΔfG°	213.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	213.90	kJ/mol	KDB
Rg	3.8000		KDB
Δc,grossH	4395.33	kJ/mol	KDB
Δc,netH	4219.313	kJ/mol	KDB
ΔfH°gas	[-15.10; 151.50]	kJ/mol
ΔfH°gas	147.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	146.90 ± 1.00	kJ/mol	NIST
ΔfH°gas	151.50	kJ/mol	NIST
ΔfH°gas	131.50 ± 4.00	kJ/mol	NIST
ΔfH°gas	-15.10	kJ/mol	NIST
ΔfH°liquid	[-58.60; 108.00]	kJ/mol
ΔfH°liquid	103.40 ± 0.92	kJ/mol	NIST
ΔfH°liquid	108.00	kJ/mol	NIST
ΔfH°liquid	87.60 ± 4.00	kJ/mol	NIST
ΔfH°liquid	-58.60	kJ/mol	NIST
ΔfusH°	9.24	kJ/mol	Joback Calculated Property
ΔvapH°	[43.20; 43.93]	kJ/mol
ΔvapH°	43.93 ± 0.42	kJ/mol	NIST
ΔvapH°	43.90	kJ/mol	NIST
ΔvapH°	43.50 ± 0.40	kJ/mol	NIST
ΔvapH°	43.50	kJ/mol	NIST
ΔvapH°	43.20	kJ/mol	NIST
ΔvapH°	43.93 ± 0.42	kJ/mol	NIST
ΔvapH°	43.90	kJ/mol	NIST
ΔvapH°	43.50 ± 0.40	kJ/mol	NIST
IE	[8.20; 8.58]	eV
IE	8.46 ± 0.00	eV	NIST
IE	8.46 ± 0.00	eV	NIST
IE	8.47	eV	NIST
IE	8.43	eV	NIST
IE	Outlier 8.20 ± 0.10	eV	NIST
IE	8.42	eV	NIST
IE	8.40 ± 0.02	eV	NIST
IE	8.28 ± 0.04	eV	NIST
IE	8.53	eV	NIST
IE	8.43 ± 0.01	eV	NIST
IE	8.42	eV	NIST
IE	8.47 ± 0.02	eV	NIST
IE	8.48	eV	NIST
IE	8.58	eV	NIST
IE	8.50	eV	NIST
IE	8.49	eV	NIST
IE	8.55	eV	NIST
IE	8.55	eV	NIST
log10WS	[-2.82; -2.70]
log10WS	-2.70		Aq. Solubility Prediction
log10WS	-2.82		Estimated Solubility
logPoct/wat	2.330		Crippen Calculated Property
McVol	95.520	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
NFPA Safety	2		KDB
Pc	[3840.00; 3998.96]	kPa
Pc	3870.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3998.96	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3840.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3990.00	kPa	KDB
Ptriple	0.01	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[125.20; 916.00]
Inp	874.35		NIST
Inp	885.00		NIST
Inp	880.00		NIST
Inp	893.00		NIST
Inp	890.50		NIST
Inp	874.50		NIST
Inp	874.40		NIST
Inp	874.90		NIST
Inp	874.00		NIST
Inp	874.35		NIST
Inp	873.00		NIST
Inp	885.00		NIST
Inp	885.00		NIST
Inp	884.00		NIST
Inp	885.00		NIST
Inp	880.00		NIST
Inp	875.00		NIST
Inp	872.00		NIST
Inp	877.80		NIST
Inp	886.00		NIST
Inp	893.00		NIST
Inp	880.00		NIST
Inp	872.00		NIST
Inp	874.50		NIST
Inp	885.00		NIST
Inp	890.50		NIST
Inp	897.30		NIST
Inp	875.00		NIST
Inp	860.90		NIST
Inp	872.00		NIST
Inp	874.50		NIST
Inp	915.00		NIST
Inp	916.00		NIST
Inp	873.00		NIST
Inp	874.40		NIST
Inp	874.70		NIST
Inp	874.90		NIST
Inp	878.00		NIST
Inp	876.00		NIST
Inp	863.00		NIST
Inp	869.00		NIST
Inp	874.00		NIST
Inp	885.00		NIST
Inp	874.00		NIST
Inp	914.00		NIST
Inp	867.00		NIST
Inp	878.00		NIST
Inp	871.00		NIST
Inp	873.00		NIST
Inp	882.00		NIST
Inp	875.00		NIST
Inp	897.00		NIST
Inp	895.00		NIST
Inp	915.00		NIST
Inp	914.00		NIST
Inp	895.00		NIST
Inp	894.00		NIST
Inp	890.00		NIST
Inp	900.00		NIST
Inp	893.00		NIST
Inp	897.00		NIST
Inp	870.00		NIST
Inp	895.20		NIST
Inp	907.00		NIST
Inp	880.00		NIST
Inp	874.00		NIST
Inp	880.30		NIST
Inp	871.00		NIST
Inp	898.00		NIST
Inp	893.00		NIST
Inp	890.00		NIST
Inp	876.00		NIST
Inp	889.00		NIST
Inp	872.00		NIST
Inp	886.00		NIST
Inp	888.00		NIST
Inp	892.60		NIST
Inp	888.00		NIST
Inp	898.00		NIST
Inp	898.00		NIST
Inp	894.00		NIST
Inp	897.00		NIST
Inp	900.02		NIST
Inp	905.00		NIST
Inp	904.00		NIST
Inp	871.00		NIST
Inp	873.00		NIST
Inp	884.00		NIST
Inp	885.00		NIST
Inp	863.00		NIST
Inp	868.00		NIST
Inp	882.00		NIST
Inp	895.00		NIST
Inp	884.00		NIST
Inp	878.00		NIST
Inp	890.00		NIST
Inp	892.00		NIST
Inp	893.00		NIST
Inp	896.00		NIST
Inp	893.00		NIST
Inp	895.00		NIST
Inp	890.00		NIST
Inp	877.00		NIST
Inp	871.00		NIST
Inp	878.00		NIST
Inp	872.00		NIST
Inp	872.00		NIST
Inp	887.00		NIST
Inp	874.00		NIST
Inp	895.00		NIST
Inp	897.00		NIST
Inp	895.00		NIST
Inp	878.00		NIST
Inp	891.40		NIST
Inp	893.00		NIST
Inp	880.00		NIST
Inp	889.00		NIST
Inp	876.00		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	870.00		NIST
Inp	897.00		NIST
Inp	881.00		NIST
Inp	873.29		NIST
Inp	892.00		NIST
Inp	875.00		NIST
Inp	877.00		NIST
Inp	875.00		NIST
Inp	893.00		NIST
Inp	895.00		NIST
Inp	872.00		NIST
Inp	895.00		NIST
Inp	877.00		NIST
Inp	873.00		NIST
Inp	880.00		NIST
Inp	875.00		NIST
Inp	878.00		NIST
Inp	878.00		NIST
Inp	880.00		NIST
Inp	883.00		NIST
Inp	874.00		NIST
Inp	893.00		NIST
Inp	866.00		NIST
Inp	869.00		NIST
Inp	896.00		NIST
Inp	897.00		NIST
Inp	911.00		NIST
Inp	879.00		NIST
Inp	867.00		NIST
Inp	895.00		NIST
Inp	892.00		NIST
Inp	889.00		NIST
Inp	891.00		NIST
Inp	897.00		NIST
Inp	910.00		NIST
Inp	881.00		NIST
Inp	895.00		NIST
Inp	893.00		NIST
Inp	878.00		NIST
Inp	886.00		NIST
Inp	904.00		NIST
Inp	903.00		NIST
Inp	883.00		NIST
Inp	887.00		NIST
Inp	904.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	875.00		NIST
Inp	887.00		NIST
Inp	890.00		NIST
Inp	862.00		NIST
Inp	871.00		NIST
Inp	868.00		NIST
Inp	875.00		NIST
Inp	876.00		NIST
Inp	880.00		NIST
Inp	886.00		NIST
Inp	879.00		NIST
Inp	900.00		NIST
Inp	871.00		NIST
Inp	900.00		NIST
Inp	871.00		NIST
Inp	Outlier 125.30		NIST
Inp	Outlier 125.20		NIST
Inp	Outlier 146.81		NIST
Inp	Outlier 135.50		NIST
Inp	Outlier 135.00		NIST
Inp	Outlier 127.70		NIST
Inp	Outlier 135.40		NIST
Inp	Outlier 127.70		NIST
Inp	875.00		NIST
Inp	Outlier 125.30		NIST
Inp	873.00		NIST
Inp	863.00		NIST
Inp	878.00		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	892.00		NIST
Inp	883.00		NIST
Ip	[1228.70; 1310.00]
Ip	1229.00		NIST
Ip	1252.00		NIST
Ip	1270.00		NIST
Ip	1250.00		NIST
Ip	1273.00		NIST
Ip	1243.00		NIST
Ip	Outlier 1291.70		NIST
Ip	Outlier 1300.00		NIST
Ip	1255.10		NIST
Ip	1283.80		NIST
Ip	1281.90		NIST
Ip	1282.60		NIST
Ip	1284.80		NIST
Ip	Outlier 1293.50		NIST
Ip	Outlier 1295.00		NIST
Ip	1228.70		NIST
Ip	1275.00		NIST
Ip	1259.00		NIST
Ip	1254.00		NIST
Ip	1248.00		NIST
Ip	1241.00		NIST
Ip	1245.00		NIST
Ip	1260.00		NIST
Ip	1251.00		NIST
Ip	1248.00		NIST
Ip	1267.00		NIST
Ip	1248.00		NIST
Ip	1262.00		NIST
Ip	1262.00		NIST
Ip	1247.00		NIST
Ip	1245.00		NIST
Ip	1244.00		NIST
Ip	1239.00		NIST
Ip	1262.00		NIST
Ip	1261.00		NIST
Ip	1285.00		NIST
Ip	1255.00		NIST
Ip	1259.00		NIST
Ip	1256.00		NIST
Ip	1265.00		NIST
Ip	1264.00		NIST
Ip	1267.00		NIST
Ip	1230.00		NIST
Ip	1262.00		NIST
Ip	1267.00		NIST
Ip	1263.00		NIST
Ip	1261.00		NIST
Ip	1264.00		NIST
Ip	1263.00		NIST
Ip	1263.00		NIST
Ip	1236.00		NIST
Ip	1264.00		NIST
Ip	1267.00		NIST
Ip	1245.00		NIST
Ip	1269.00		NIST
Ip	1275.00		NIST
Ip	1229.00		NIST
Ip	1229.00		NIST
Ip	1262.00		NIST
Ip	1241.00		NIST
Ip	1247.00		NIST
Ip	1252.00		NIST
Ip	1252.00		NIST
Ip	1264.00		NIST
Ip	1248.00		NIST
Ip	1268.00		NIST
Ip	1277.00		NIST
Ip	1270.00		NIST
Ip	1239.00		NIST
Ip	1249.00		NIST
Ip	1257.00		NIST
Ip	1248.00		NIST
Ip	1250.00		NIST
Ip	1252.00		NIST
Ip	1273.00		NIST
Ip	1240.00		NIST
Ip	1273.00		NIST
Ip	1273.00		NIST
Ip	1255.00		NIST
Ip	1240.00		NIST
Ip	1242.00		NIST
Ip	1243.00		NIST
Ip	1252.00		NIST
Ip	1253.00		NIST
Ip	1263.00		NIST
Ip	1262.00		NIST
Ip	1248.00		NIST
Ip	Outlier 1310.00		NIST
Ip	1254.00		NIST
Ip	1266.00		NIST
Ip	1274.00		NIST
Ip	1255.00		NIST
Ip	1272.00		NIST
Ip	1262.00		NIST
Ip	1272.00		NIST
Ip	1241.00		NIST
Ip	1267.00		NIST
Ip	1245.00		NIST
Ip	1285.00		NIST
Ip	1264.00		NIST
Ip	1263.00		NIST
Ip	1266.00		NIST
Ip	1262.00		NIST
S°gas	345.10 ± 2.10	J/mol×K	NIST
S°liquid	[237.57; 240.50]	J/mol×K
S°liquid	240.50	J/mol×K	NIST
S°liquid	237.57	J/mol×K	NIST
S°liquid	237.60	J/mol×K	NIST
S°liquid	237.57	J/mol×K	NIST
Tboil	[413.15; 420.65]	K
Tboil	418.31	K	ChemSep v8.3 pure component data Compiled value
Tboil	418.30	K	KDB
Tboil	418.40	K	NIST
Tboil	418.35	K	NIST
Tboil	420.65 ± 5.00	K	NIST
Tboil	417.65 ± 5.00	K	NIST
Tboil	418.25 ± 1.50	K	NIST
Tboil	418.75 ± 0.30	K	NIST
Tboil	418.15 ± 1.00	K	NIST
Tboil	418.65 ± 2.00	K	NIST
Tboil	418.29 ± 0.20	K	NIST
Tboil	418.45 ± 0.20	K	NIST
Tboil	418.45 ± 0.30	K	NIST
Tboil	418.65 ± 1.00	K	NIST
Tboil	418.95 ± 0.30	K	NIST
Tboil	419.15 ± 1.50	K	NIST
Tboil	418.35 ± 0.30	K	NIST
Tboil	418.25 ± 0.30	K	NIST
Tboil	419.00 ± 0.50	K	NIST
Tboil	419.00 ± 0.50	K	NIST
Tboil	416.00 ± 4.00	K	NIST
Tboil	Outlier 413.15 ± 2.00	K	NIST
Tc	[635.20; 647.59]	K
Tc	635.20	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	647.59	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	636.00	K	ChemSep v8.3 pure component data Compiled value
Tc	647.00	K	KDB
Tfus	[197.55; 242.55]	K
Tfus	242.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	242.54	K	ChemSep v8.3 pure component data Compiled value
Tfus	242.50	K	KDB
Tfus	242.55	K	NIST
Tfus	242.38 ± 0.40	K	NIST
Tfus	242.47 ± 0.15	K	NIST
Tfus	242.47 ± 0.20	K	NIST
Tfus	242.50 ± 0.20	K	NIST
Tfus	242.50 ± 0.20	K	NIST
Tfus	Outlier 197.55 ± 0.05	K	NIST
Tfus	228.15 ± 5.00	K	NIST
Tfus	242.25 ± 0.50	K	NIST
Tfus	242.55 ± 0.20	K	NIST
Tfus	239.85 ± 0.40	K	NIST
Ttriple	[242.47; 242.54]	K
Ttriple	242.48	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	Outlier 242.54	K	ChemSep v8.3 pure component data Compiled value
Ttriple	242.47 ± 0.07	K	NIST
Ttriple	242.47 ± 0.10	K	NIST
Ttriple	242.47 ± 0.10	K	NIST
Ttriple	242.47 ± 0.07	K	NIST
UQi	3.30		ChemSep v8.3 pure component data Compiled value
URi	4.37		ChemSep v8.3 pure component data Compiled value
Vc	[0.347; 0.352]	m3/kmol
Vc	0.347	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.352	m3/kmol	ChemSep v8.3 pure component data Compiled value
VCOSTALD	0.35	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.24		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	0.2560000		ChemSep v8.3 pure component data Compiled value
Zra	[0.26; 0.26]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	151.29 ± 0.76	J/mol×K	373.15	NIST
Cp,liquid	[168.80; 235.60]	J/mol×K	[250.00; 300.00]
Cp,liquid	168.80	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	171.60	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	174.40	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
Cp,liquid	175.30	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	177.20	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	180.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	235.60	J/mol×K	298.00	NIST
Cp,liquid	182.20	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
Cp,liquid	183.20	J/mol×K	298.15	NIST
Cp,liquid	182.84	J/mol×K	298.15	NIST
Cp,liquid	182.84	J/mol×K	298.15	NIST
Cp,liquid	182.60	J/mol×K	298.16	NIST
Cp,liquid	179.90	J/mol×K	298.50	NIST
Cp,liquid	182.80	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
η	[0.0003490; 0.0007490]	Pa×s	[293.15; 363.15]
η	0.0007490	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0006990	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0006540	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0005770	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0005130	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0004620	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0004190	Pa×s	343.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0003810	Pa×s	353.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0003490	Pa×s	363.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
ΔfusH	[10.95; 10.96]	kJ/mol	[242.27; 242.47]
ΔfusH	10.96	kJ/mol	242.27	NIST
ΔfusH	10.95	kJ/mol	242.27	NIST
ΔfusH	10.95	kJ/mol	242.27	NIST
ΔfusH	10.96	kJ/mol	242.30	NIST
ΔfusH	10.95	kJ/mol	242.30	NIST
ΔfusH	10.95	kJ/mol	242.47	NIST
ΔfusH	10.95	kJ/mol	242.47	NIST
ΔvapH	[36.82; 43.10]	kJ/mol	[289.50; 418.20]
ΔvapH	42.50	kJ/mol	289.50	NIST
ΔvapH	42.50	kJ/mol	319.50	NIST
ΔvapH	40.20	kJ/mol	347.50	NIST
ΔvapH	43.10	kJ/mol	360.00	NIST
ΔvapH	41.50	kJ/mol	376.50	NIST
ΔvapH	36.82	kJ/mol	418.20	KDB
Pvap	[5.00; 25.00]	kPa	[332.40; 372.40]
Pvap	5.00	kPa	332.40	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	7.50	kPa	341.40	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	10.00	kPa	348.30	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	12.50	kPa	353.90	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	15.00	kPa	358.50	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	17.50	kPa	362.60	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	20.00	kPa	366.20	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	22.50	kPa	369.40	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap	25.00	kPa	372.40	Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
n0	[1.52910; 1.55330]		[283.15; 323.15]
n0	1.55330		283.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.55050		288.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.54600		293.15	Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
n0	1.54600		293.15	A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n0	1.54600		293.15	Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
n0	1.54720		293.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.54600		298.15	The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
n0	1.54400		298.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.54660		298.15	Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
n0	1.54395		298.15	KDB
n0	1.54380		298.15	Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
n0	1.54560		298.15	Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
n0	1.54090		303.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.54450		303.15	Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
n0	1.53800		308.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.54370		308.15	Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
n0	1.54290		313.15	Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
n0	1.53520		313.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.53210		318.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
n0	1.52910		323.15	Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
ρl	[888.47; 906.26]	kg/m3	[293.00; 313.15]
ρl	906.00	kg/m3	293.00	KDB
ρl	906.26	kg/m3	293.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρl	901.94	kg/m3	298.15	Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
ρl	900.52	kg/m3	298.15	Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
ρl	897.39	kg/m3	303.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρl	888.47	kg/m3	313.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ΔfusS	[45.16; 45.32]	J/mol×K	[242.27; 242.47]
ΔfusS	45.32	J/mol×K	242.27	NIST
ΔfusS	45.16	J/mol×K	242.27	NIST
ΔfusS	45.16	J/mol×K	242.27	NIST
ΔfusS	45.16	J/mol×K	242.47	NIST
ΔfusS	45.20	J/mol×K	242.47	NIST
γ	0.03	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[59.51; 325.02]	J/mol×K	[100.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.78067e+01
Coefficient B			-5.50425e+02
Coefficient C			6.04600e+00
Coefficient D			-9.50882e-05
Coefficient E			2.29476e-08
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	59.51	J/mol×K	100.00	Calculated Property
Cp,gas	105.72	J/mol×K	255.56	Calculated Property
Cp,gas	164.71	J/mol×K	411.11	Calculated Property
Cp,gas	210.46	J/mol×K	566.67	Calculated Property
Cp,gas	244.07	J/mol×K	722.22	Calculated Property
Cp,gas	269.08	J/mol×K	877.78	Calculated Property
Cp,gas	288.15	J/mol×K	1033.33	Calculated Property
Cp,gas	303.09	J/mol×K	1188.89	Calculated Property
Cp,gas	315.10	J/mol×K	1344.44	Calculated Property
Cp,gas	325.02	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[167.61; 228.08]	J/mol×K	[242.54; 418.31]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.34310e+02
Coefficient B			-9.99160e+01
Coefficient C			2.58574e+00
Coefficient D			5.82940e-03
Coefficient E			-1.39720e-06
Temperature range, min.			242.54
Temperature range, max.			418.31
Cp,liquid	167.61	J/mol×K	242.54	Calculated Property
Cp,liquid	172.26	J/mol×K	262.07	Calculated Property
Cp,liquid	177.33	J/mol×K	281.60	Calculated Property
Cp,liquid	182.86	J/mol×K	301.13	Calculated Property
Cp,liquid	188.89	J/mol×K	320.66	Calculated Property
Cp,liquid	195.47	J/mol×K	340.19	Calculated Property
Cp,liquid	202.63	J/mol×K	359.72	Calculated Property
Cp,liquid	210.42	J/mol×K	379.25	Calculated Property
Cp,liquid	218.89	J/mol×K	398.78	Calculated Property
Cp,liquid	228.08	J/mol×K	418.31	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0019207; 0.0001498]	Pa×s	[242.54; 508.80]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.47170e+01
Coefficient B			1.82400e+03
Coefficient C			1.99770e+00
Coefficient D			-4.79330e-07
Coefficient E			2.00000e+00
Temperature range, min.			242.54
Temperature range, max.			508.80
η	0.0019207	Pa×s	242.54	Calculated Property
η	0.0010594	Pa×s	272.12	Calculated Property
η	0.0006693	Pa×s	301.71	Calculated Property
η	0.0004660	Pa×s	331.29	Calculated Property
η	0.0003486	Pa×s	360.88	Calculated Property
η	0.0002753	Pa×s	390.46	Calculated Property
η	0.0002266	Pa×s	420.05	Calculated Property
η	0.0001927	Pa×s	449.63	Calculated Property
η	0.0001681	Pa×s	479.22	Calculated Property
η	0.0001498	Pa×s	508.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[48.87; 14.18]	kJ/mol	[242.54; 615.29]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			1.11062e+02
Coefficient B			3.42928e+00
Coefficient C			-6.06105e+00
Coefficient D			4.60558e+00
Coefficient E			-1.40823e+00
Critical temperature, Tc (K)			6.36000e+02
Temperature range, min.			242.54
Temperature range, max.			615.29
ΔvapH	48.87	kJ/mol	242.54	Calculated Property
ΔvapH	45.31	kJ/mol	283.96	Calculated Property
ΔvapH	42.35	kJ/mol	325.37	Calculated Property
ΔvapH	39.74	kJ/mol	366.79	Calculated Property
ΔvapH	37.25	kJ/mol	408.21	Calculated Property
ΔvapH	34.66	kJ/mol	449.62	Calculated Property
ΔvapH	31.74	kJ/mol	491.04	Calculated Property
ΔvapH	28.12	kJ/mol	532.46	Calculated Property
ΔvapH	23.08	kJ/mol	573.87	Calculated Property
ΔvapH	14.18	kJ/mol	615.29	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[305.95; 447.65]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39212e+01
Coefficient B			-3.31078e+03
Coefficient C			-6.31110e+01
Temperature range, min.			305.95
Temperature range, max.			447.65
Pvap	1.33	kPa	305.95	Calculated Property
Pvap	3.06	kPa	321.69	Calculated Property
Pvap	6.38	kPa	337.44	Calculated Property
Pvap	12.27	kPa	353.18	Calculated Property
Pvap	22.09	kPa	368.93	Calculated Property
Pvap	37.53	kPa	384.67	Calculated Property
Pvap	60.69	kPa	400.42	Calculated Property
Pvap	94.02	kPa	416.16	Calculated Property
Pvap	140.31	kPa	431.91	Calculated Property
Pvap	202.64	kPa	447.65	Calculated Property
Pvap	[7.88e-03; 3840.00]	kPa	[242.54; 531.41]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			3.92941e+02
Coefficient B			-1.90173e+04
Coefficient C			-5.89629e+01
Coefficient D			7.47957e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 636 K.
Temperature range, min.			242.54
Temperature range, max.			531.41
Pvap	7.88e-03	kPa	242.54	Calculated Property
Pvap	0.17	kPa	274.64	Calculated Property
Pvap	1.43	kPa	306.73	Calculated Property
Pvap	6.78	kPa	338.83	Calculated Property
Pvap	23.05	kPa	370.93	Calculated Property
Pvap	65.73	kPa	403.02	Calculated Property
Pvap	174.20	kPa	435.12	Calculated Property
Pvap	460.56	kPa	467.22	Calculated Property
Pvap	1276.33	kPa	499.31	Calculated Property
Pvap	3840.00	kPa	531.41	Calculated Property
Pvap	[0.01; 4030.19]	kPa	[242.54; 648.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.60058e+01
Coefficient B			-8.11907e+03
Coefficient C			-1.04313e+01
Coefficient D			5.61169e-06
Coefficient E			0.00000e+00
Temperature range, min.			242.54
Temperature range, max.			648.00
Pvap	0.01	kPa	242.54	Calculated Property
Pvap	0.44	kPa	287.59	Calculated Property
Pvap	5.17	kPa	332.64	Calculated Property
Pvap	30.25	kPa	377.69	Calculated Property
Pvap	112.99	kPa	422.74	Calculated Property
Pvap	312.86	kPa	467.80	Calculated Property
Pvap	705.72	kPa	512.85	Calculated Property
Pvap	1380.25	kPa	557.90	Calculated Property
Pvap	2442.56	kPa	602.95	Calculated Property
Pvap	4030.19	kPa	648.00	Calculated Property
Pvap	[1.34; 13.29]	kPa	[305.60; 355.34]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39521e+01
Coefficient B			-3.36156e+03
Coefficient C			-5.95510e+01
Reference			Chaiyavech and Van Winkle, 1959
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			305.60
Temperature range, max.			355.34
Pvap	1.34	kPa	305.60	Calculated Property
Pvap	1.80	kPa	311.13	Calculated Property
Pvap	2.40	kPa	316.65	Calculated Property
Pvap	3.17	kPa	322.18	Calculated Property
Pvap	4.12	kPa	327.71	Calculated Property
Pvap	5.31	kPa	333.23	Calculated Property
Pvap	6.77	kPa	338.76	Calculated Property
Pvap	8.55	kPa	344.29	Calculated Property
Pvap	10.71	kPa	349.81	Calculated Property
Pvap	13.29	kPa	355.34	Calculated Property
Pvap	[1.09; 100.29]	kPa	[303.07; 417.92]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43209e+01
Coefficient B			-3.51158e+03
Coefficient C			-5.63790e+01
Reference			Dreyer, Martin, et al., 1955
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			303.07
Temperature range, max.			417.92
Pvap	1.09	kPa	303.07	Calculated Property
Pvap	2.20	kPa	315.83	Calculated Property
Pvap	4.14	kPa	328.59	Calculated Property
Pvap	7.38	kPa	341.35	Calculated Property
Pvap	12.51	kPa	354.11	Calculated Property
Pvap	20.31	kPa	366.88	Calculated Property
Pvap	31.75	kPa	379.64	Calculated Property
Pvap	47.96	kPa	392.40	Calculated Property
Pvap	70.30	kPa	405.16	Calculated Property
Pvap	100.29	kPa	417.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[946.09; 388.96]	kg/m3	[242.54; 636.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.01867e+01
Coefficient B			2.31390e-01
Coefficient C			6.40770e+02
Coefficient D			2.63510e-01
Comment			Range stopped at Tc; ChemSep gives it to 640.76 K.
Temperature range, min.			242.54
Temperature range, max.			636.00
ρl	946.09	kg/m3	242.54	Calculated Property
ρl	909.93	kg/m3	286.26	Calculated Property
ρl	871.91	kg/m3	329.98	Calculated Property
ρl	831.57	kg/m3	373.69	Calculated Property
ρl	788.27	kg/m3	417.41	Calculated Property
ρl	740.99	kg/m3	461.13	Calculated Property
ρl	688.02	kg/m3	504.85	Calculated Property
ρl	625.95	kg/m3	548.56	Calculated Property
ρl	545.91	kg/m3	592.28	Calculated Property
ρl	388.96	kg/m3	636.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.03]	N/m	[273.15; 418.31]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			1.43560e-02
Coefficient B			-4.15600e+02
Coefficient C			1.41760e-01
Coefficient D			-1.14410e-02
Coefficient E			6.32140e-06
Temperature range, min.			273.15
Temperature range, max.			418.31
γ	0.03	N/m	273.15	Calculated Property
γ	0.03	N/m	289.28	Calculated Property
γ	0.03	N/m	305.41	Calculated Property
γ	0.03	N/m	321.54	Calculated Property
γ	0.03	N/m	337.67	Calculated Property
γ	0.03	N/m	353.79	Calculated Property
γ	0.03	N/m	369.92	Calculated Property
γ	0.03	N/m	386.05	Calculated Property
γ	0.03	N/m	402.18	Calculated Property
γ	0.03	N/m	418.31	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[242.54; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.02290e-02
Coefficient B			4.00850e-01
Coefficient C			5.35560e+02
Coefficient D			7.04200e+05
Temperature range, min.			242.54
Temperature range, max.			1000.00
λgas	0.01	W/m×K	242.54	Calculated Property
λgas	0.01	W/m×K	326.70	Calculated Property
λgas	0.02	W/m×K	410.86	Calculated Property
λgas	0.02	W/m×K	495.03	Calculated Property
λgas	0.03	W/m×K	579.19	Calculated Property
λgas	0.04	W/m×K	663.35	Calculated Property
λgas	0.05	W/m×K	747.51	Calculated Property
λgas	0.06	W/m×K	831.68	Calculated Property
λgas	0.06	W/m×K	915.84	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[242.54; 598.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-7.18170e-02
Coefficient B			-3.00130e+01
Coefficient C			-1.02620e+00
Coefficient D			-1.56230e-03
Coefficient E			2.76740e-07
Temperature range, min.			242.54
Temperature range, max.			598.15
λliquid	0.15	W/m×K	242.54	Calculated Property
λliquid	0.14	W/m×K	282.05	Calculated Property
λliquid	0.13	W/m×K	321.56	Calculated Property
λliquid	0.12	W/m×K	361.08	Calculated Property
λliquid	0.11	W/m×K	400.59	Calculated Property
λliquid	0.11	W/m×K	440.10	Calculated Property
λliquid	0.10	W/m×K	479.61	Calculated Property
λliquid	0.09	W/m×K	519.13	Calculated Property
λliquid	0.08	W/m×K	558.64	Calculated Property
λliquid	0.08	W/m×K	598.15	Calculated Property

Similar Compounds

Find more compounds similar to Styrene.

Mixtures

• Benzene, nitro- + Styrene
• Nitrogen + Styrene
• Styrene + Oxygen
• Nitrogen + Styrene + Oxygen
• 1,3-Dioxolan-2-one, 4-methyl- + Styrene
• Styrene + Cyclohexanone
• Styrene + Dimethyl Sulfoxide
• Styrene + Ethyl Acetate
• Benzene + Styrene
• Styrene + Formamide, N,N-dimethyl- + Ethyl Acetate
• Benzene + Styrene + Formamide, N,N-dimethyl-
• Styrene + Carbon dioxide
• Styrene + Carbonic acid, dimethyl ester
• Styrene + 1-Butanol, 3-methyl-, acetate
• Styrene + Carbon dioxide + Benzene, ethyl-
• Styrene + Carbon dioxide + Safrole
• Styrene + Water
• Styrene + Benzene, ethyl-
• Styrene + Thiophene, tetrahydro-, 1,1-dioxide
• Styrene + Benzene, ethyl- + Thiophene, tetrahydro-, 1,1-dioxide

Find more mixtures with Styrene.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
• Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
• Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
• Binary and ternary vapor-liquid equilibrium data of the system ethylbenzene + styrene + 3-methyl-N-butylpyridinium tetracyanoborate at vacuum conditions and liquid-liquid equilibrium data of their binary systems
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Gas solubilities of nitrogen or oxygen in benzene, divinylbenzene, styrene and of an equimolar (N2:O2) mixture in styrene at (293-313) K
• Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
• Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
• The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
• Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
• Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
• Binary and ternary LLE data of the system (ethylbenzene + styrene + 1-ethyl-3-methylimidazolium thiocyanate) and binary VLE data of the system (styrene + 1-ethyl-3-methylimidazolium thiocyanate)
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Liquid-liquid extraction of styrene from ethylbenzene using ionic liquids
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Vapour-liquid phase boundaries including the near critical regions of the (CO2 + styrene, CO2 + 1,4-dioxane, and CO2 + N,N-dimethylformamide) systems
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
• Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Binary and Ternary Vapor-Liquid Equilibrium Data of the System (Ethylbenzene + Styrene + 4-Methyl-N-butylpyridinium Tetrafluoroborate) at Vacuum Conditions and Liquid-Liquid Equilibrium Data of Their Binary Systems
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Phase Equilibria of the Systems CO2 + Styrene, CO2 + Safrole, and CO2 + Styrene + Safrole
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Limiting Binary Diffusivities of Aniline, Styrene, and Mesitylene in Supercritical Carbon Dioxide
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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