Benzene, 1,1'-oxybis- (CAS 101-84-8)

InChI

InChI=1S/C12H10O/c1-3-7-11(8-4-1)13-12-9-5-2-6-10-12/h1-10H

InChI Key

USIUVYZYUHIAEV-UHFFFAOYSA-N

Formula

C12H10O

SMILES

c1ccc(Oc2ccccc2)cc1

Molecular Weight¹

170.21

CAS

101-84-8

Other Names

1,1'-OXYBIS-BENZENE
1,1'-Oxybisbenzene
Benzene, phenoxy-
Biphenyl oxide
Chemcryl JK-EB
Ether, diphenyl-
Geranium crystals
NSC 19311
Oxybisbenzene
Oxydiphenyl
PHENOXY BENZENE
Phenyl oxide
diphenyl ether
diphenyl oxide
phenoxybenzene
phenyl ether

ω : Acentric Factor.
T_ig : Autoignition Temperature (K).
Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
Δ_cH°_solid : Standard solid 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).
C_p,solid : Solid phase heat capacity (J/mol×K).
μ : Dipole Moment (debye).
η : Dynamic viscosity (Pa×s).
ε_r : Dielectric Constant (Relative permittivity).
T_flash,cc : Flash Point (Closed Cup Method) (K).
Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
Δ_fH°_solid : Solid 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).
γ : Surface Tension (N/m).
S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
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).
Z_c : Critical Compressibility.
Z_ra : Rackett Parameter.
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties

Property	Value	Unit	Source
ω	[0.4389; 0.4400]
ω	0.4400		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4389		ChemSep v8.3 pure component data Compiled value
ω	0.4400		KDB
T_ig	891.15	K	NCMS SOLV-DB
Δ_cH°_liquid	-6113.70 ± 3.80	kJ/mol	NIST
Δ_cH°_solid	-6119.24 ± 0.88	kJ/mol	NIST
μ	[1.10; 1.16]	debye
μ	1.16	debye	ChemSep v8.3 pure component data Compiled value
μ	1.10	debye	KDB
ε_r	3.87		NCMS SOLV-DB
T_flash,cc	369.15	K	NCMS SOLV-DB
Δ_fG°	175.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	[42.30; 49.99]	kJ/mol
Δ_fH°_gas	42.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	49.99	kJ/mol	KDB
Δ_fH°_solid	-32.11 ± 0.93	kJ/mol	NIST
Δ_fusH°	17.12	kJ/mol	Standard enthalpy of formation of diphenyl oxide
Δ_vapH°	[64.90; 67.10]	kJ/mol
Δ_vapH°	66.90	kJ/mol	NCMS SOLV-DB
Δ_vapH°	67.10	kJ/mol	NIST
Δ_vapH°	65.00	kJ/mol	NIST
Δ_vapH°	66.90 ± 0.30	kJ/mol	NIST
Δ_vapH°	66.10 ± 0.40	kJ/mol	NIST
Δ_vapH°	64.90 ± 2.10	kJ/mol	NIST
IE	[8.00; 8.82]	eV
IE	8.09	eV	NIST
IE	8.00	eV	NIST
IE	8.09 ± 0.03	eV	NIST
IE	8.10	eV	NIST
IE	8.82 ± 0.05	eV	NIST
log₁₀WS	[-3.96; -3.93]
log₁₀WS	-3.93		Aq. Solubility Prediction
log₁₀WS	-3.96		Estimated Solubility
logP_oct/wat	4.210		NCMS SOLV-DB
McVol	138.290	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=1); %!d(float64=1)]
NFPA Fire	1		KDB
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
P_c	[3120.00; 3141.08]	kPa
P_c	3141.08	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	3120.00	kPa	ChemSep v8.3 pure component data Compiled value
P_c	3140.00	kPa	KDB
P_c	3141.07 ± 202.65	kPa	NIST
P_triple	7.09e-03	kPa	ChemSep v8.3 pure component data Compiled value
I_np	[241.16; 1405.00]
I_np	1389.90		NIST
I_np	1378.00		NIST
I_np	1380.00		NIST
I_np	1396.00		NIST
I_np	1376.30		NIST
I_np	1366.80		NIST
I_np	1370.00		NIST
I_np	1370.90		NIST
I_np	1366.40		NIST
I_np	1381.70		NIST
I_np	1393.70		NIST
I_np	1380.10		NIST
I_np	1384.60		NIST
I_np	1404.00		NIST
I_np	1405.00		NIST
I_np	1372.00		NIST
I_np	1396.00		NIST
I_np	1386.00		NIST
I_np	1364.00		NIST
I_np	1372.00		NIST
I_np	1356.90		NIST
I_np	1372.60		NIST
I_np	1371.80		NIST
I_np	1376.20		NIST
I_np	1386.00		NIST
I_np	1379.00		NIST
I_np	1363.00		NIST
I_np	1376.00		NIST
I_np	Outlier 241.70		NIST
I_np	Outlier 241.16		NIST
I_np	Outlier 241.70		NIST
I_np	1378.00		NIST
I_np	1396.00		NIST
I_np	1366.40		NIST
I_p	[1991.00; 2055.00]
I_p	2017.00		NIST
I_p	2017.00		NIST
I_p	2026.00		NIST
I_p	1991.00		NIST
I_p	2038.00		NIST
I_p	2017.00		NIST
I_p	1991.00		NIST
I_p	2055.00		NIST
I_p	2026.00		NIST
S°_{solid,1 bar}	233.91	J/mol×K	NIST
T_boil	[523.65; 532.50]	K
T_boil	531.46	K	ChemSep v8.3 pure component data Compiled value
T_boil	531.20	K	KDB
T_boil	531.21	K	NCMS SOLV-DB
T_boil	532.20	K	NIST
T_boil	531.10	K	NIST
T_boil	Outlier 523.65 ± 1.50	K	NIST
T_boil	531.46 ± 0.07	K	NIST
T_boil	532.50 ± 0.50	K	NIST
T_c	[766.00; 788.15]	K
T_c	767.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
T_c	766.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	767.15	K	ChemSep v8.3 pure component data Compiled value
T_c	766.80	K	KDB
T_c	766.80 ± 1.00	K	NIST
T_c	Outlier 788.15 ± 2.00	K	NIST
T_c	767.20 ± 1.00	K	NIST
T_fus	[299.90; 300.65]	K
T_fus	300.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
T_fus	300.15	K	ChemSep v8.3 pure component data Compiled value
T_fus	300.02	K	KDB
T_fus	300.60	K	Aq. Solubility Prediction
T_fus	300.02	K	NCMS SOLV-DB
T_fus	300.58 ± 0.20	K	NIST
T_fus	300.04 ± 0.01	K	NIST
T_fus	300.00 ± 0.02	K	NIST
T_fus	299.90 ± 0.02	K	NIST
T_fus	300.15 ± 1.00	K	NIST
T_fus	300.05 ± 0.05	K	NIST
T_fus	299.90 ± 0.40	K	NIST
T_fus	299.90 ± 0.30	K	NIST
T_fus	300.20 ± 0.20	K	NIST
T_triple	[300.01; 300.03]	K
T_triple	300.03	K	ChemSep v8.3 pure component data Compiled value
T_triple	300.01 ± 0.00	K	NIST
T_triple	300.03 ± 0.01	K	NIST
T_triple	300.03 ± 0.01	K	NIST
U_Qi	4.48		ChemSep v8.3 pure component data Compiled value
U_Ri	6.29		ChemSep v8.3 pure component data Compiled value
V_c	[0.504; 0.545]	m³/kmol
V_c	0.529	m³/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
V_c	0.504	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
V_c	0.545	m³/kmol	ChemSep v8.3 pure component data Compiled value
Z_c	0.2430000		ChemSep v8.3 pure component data Compiled value
Z_ra	0.24		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,solid	[215.90; 216.56]	J/mol×K	[298.15; 298.50]
C_p,solid	216.56	J/mol×K	298.15	NIST
C_p,solid	216.56	J/mol×K	298.15	NIST
C_p,solid	215.90	J/mol×K	298.50	NIST
Δ_fusH	[16.51; 17.22]	kJ/mol	[300.00; 300.40]

Δ_fusH	17.21	kJ/mol	300.00	NIST
Δ_fusH	17.21	kJ/mol	300.00	NIST
Δ_fusH	17.22	kJ/mol	300.02	NIST
Δ_fusH	17.21	kJ/mol	300.03	NIST
Δ_fusH	17.21	kJ/mol	300.03	NIST
Δ_fusH	16.51	kJ/mol	300.40	NIST
Δ_vapH	[48.20; 64.20]	kJ/mol	[323.00; 510.50]
Δ_vapH	64.20	kJ/mol	323.00	NIST
Δ_vapH	53.00	kJ/mol	510.50	NIST
Δ_vapH	48.20	kJ/mol	510.50	NIST
P_vap	[2.84e-03; 0.09]	kPa	[298.15; 343.70]

P_vap	2.84e-03	kPa	298.15	NCMS SOLV-DB
P_vap	2.93e-03	kPa	299.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	4.26e-03	kPa	303.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	5.31e-03	kPa	305.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	6.46e-03	kPa	308.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	7.44e-03	kPa	310.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	9.68e-03	kPa	313.40	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.01	kPa	315.30	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.02	kPa	319.40	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.02	kPa	323.40	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.03	kPa	327.40	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.03	kPa	328.90	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.04	kPa	331.50	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.05	kPa	335.50	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.06	kPa	339.60	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
P_vap	0.09	kPa	343.70	Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
n₀	1.57600		298.15	NCMS SOLV-DB
ρ_l	[1005.20; 1066.00]	kg/m³	[303.00; 373.15]

ρ_l	1066.00	kg/m³	303.00	KDB
ρ_l	1065.50	kg/m³	303.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1061.20	kg/m³	308.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1056.90	kg/m³	313.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1048.20	kg/m³	323.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1039.60	kg/m³	333.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1030.90	kg/m³	343.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1022.30	kg/m³	353.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1013.70	kg/m³	363.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
ρ_l	1005.20	kg/m³	373.15	Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
Δ_fusS	[57.38; 57.38]	J/mol×K	[300.02; 300.03]
Δ_fusS	57.38	J/mol×K	300.02	NIST
Δ_fusS	57.38	J/mol×K	300.03	NIST
Δ_fusS	57.38	J/mol×K	300.03	NIST
γ	0.04	N/m	298.15	NCMS SOLV-DB
λ_liquid	[0.13; 0.15]	W/m×K	[303.15; 343.15]

λ_liquid	0.13	W/m×K	303.15	Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
λ_liquid	0.13	W/m×K	313.15	Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
λ_liquid	0.14	W/m×K	323.15	Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
λ_liquid	0.14	W/m×K	333.15	Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
λ_liquid	0.15	W/m×K	343.15	Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[141.61; 495.94]	J/mol×K	[255.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,gas in J/mol×K, T in K
Coefficient A			5.50000e+01
Coefficient B			-5.00000e+02
Coefficient C			6.42224e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00

C_p,gas	141.61	J/mol×K	255.00	Calculated Property
C_p,gas	227.61	J/mol×K	393.33	Calculated Property
C_p,gas	295.28	J/mol×K	531.67	Calculated Property
C_p,gas	346.77	J/mol×K	670.00	Calculated Property
C_p,gas	386.52	J/mol×K	808.33	Calculated Property
C_p,gas	417.88	J/mol×K	946.67	Calculated Property
C_p,gas	443.16	J/mol×K	1085.00	Calculated Property
C_p,gas	463.92	J/mol×K	1223.33	Calculated Property
C_p,gas	481.26	J/mol×K	1361.67	Calculated Property
C_p,gas	495.94	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[268.47; 389.33]	J/mol×K	[300.03; 570.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is C_p,liquid in J/mol×K, T in K
Coefficient A			1.34160e+02
Coefficient B			4.47670e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			300.03
Temperature range, max.			570.00

C_p,liquid	268.47	J/mol×K	300.03	Calculated Property
C_p,liquid	281.90	J/mol×K	330.03	Calculated Property
C_p,liquid	295.33	J/mol×K	360.02	Calculated Property
C_p,liquid	308.76	J/mol×K	390.02	Calculated Property
C_p,liquid	322.19	J/mol×K	420.02	Calculated Property
C_p,liquid	335.62	J/mol×K	450.01	Calculated Property
C_p,liquid	349.05	J/mol×K	480.01	Calculated Property
C_p,liquid	362.47	J/mol×K	510.01	Calculated Property
C_p,liquid	375.90	J/mol×K	540.00	Calculated Property
C_p,liquid	389.33	J/mol×K	570.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0041243; 0.0001134]	Pa×s	[293.15; 613.44]	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			-1.23730e+01
Coefficient B			2.01750e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.15
Temperature range, max.			613.44

η	0.0041243	Pa×s	293.15	Calculated Property
η	0.0019579	Pa×s	328.74	Calculated Property
η	0.0010751	Pa×s	364.33	Calculated Property
η	0.0006568	Pa×s	399.91	Calculated Property
η	0.0004349	Pa×s	435.50	Calculated Property
η	0.0003065	Pa×s	471.09	Calculated Property
η	0.0002269	Pa×s	506.68	Calculated Property
η	0.0001747	Pa×s	542.26	Calculated Property
η	0.0001389	Pa×s	577.85	Calculated Property
η	0.0001134	Pa×s	613.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[58.55; 6.35]	kJ/mol	[300.03; 766.80]	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 Δ_vapH in kJ/mol, T in K
Coefficient A			6.82430e+01
Coefficient B			3.08770e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.67150e+02
Temperature range, min.			300.03
Temperature range, max.			766.80

Δ_vapH	58.55	kJ/mol	300.03	Calculated Property
Δ_vapH	56.46	kJ/mol	351.89	Calculated Property
Δ_vapH	54.18	kJ/mol	403.76	Calculated Property
Δ_vapH	51.67	kJ/mol	455.62	Calculated Property
Δ_vapH	48.84	kJ/mol	507.48	Calculated Property
Δ_vapH	45.59	kJ/mol	559.35	Calculated Property
Δ_vapH	41.73	kJ/mol	611.21	Calculated Property
Δ_vapH	36.83	kJ/mol	663.07	Calculated Property
Δ_vapH	29.76	kJ/mol	714.94	Calculated Property
Δ_vapH	6.35	kJ/mol	766.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.65]	kPa	[396.23; 565.91]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.44628e+01
Coefficient B			-4.38113e+03
Coefficient C			-8.71630e+01
Temperature range, min.			396.23
Temperature range, max.			565.91

P_vap	1.33	kPa	396.23	Calculated Property
P_vap	3.01	kPa	415.08	Calculated Property
P_vap	6.23	kPa	433.94	Calculated Property
P_vap	11.94	kPa	452.79	Calculated Property
P_vap	21.49	kPa	471.64	Calculated Property
P_vap	36.61	kPa	490.50	Calculated Property
P_vap	59.47	kPa	509.35	Calculated Property
P_vap	92.68	kPa	528.20	Calculated Property
P_vap	139.26	kPa	547.06	Calculated Property
P_vap	202.65	kPa	565.91	Calculated Property
P_vap	[7.09e-03; 3097.10]	kPa	[300.03; 766.80]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			5.30612e+01
Coefficient B			-8.58550e+03
Coefficient C			-5.15380e+00
Coefficient D			1.99830e-18
Coefficient E			6.00000e+00
Temperature range, min.			300.03
Temperature range, max.			766.80

P_vap	7.09e-03	kPa	300.03	Calculated Property
P_vap	0.21	kPa	351.89	Calculated Property
P_vap	2.41	kPa	403.76	Calculated Property
P_vap	14.67	kPa	455.62	Calculated Property
P_vap	58.68	kPa	507.48	Calculated Property
P_vap	175.28	kPa	559.35	Calculated Property
P_vap	426.16	kPa	611.21	Calculated Property
P_vap	897.30	kPa	663.07	Calculated Property
P_vap	1715.68	kPa	714.94	Calculated Property
P_vap	3097.10	kPa	766.80	Calculated Property
P_vap	[26.55; 133.31]	kPa	[477.36; 544.09]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.41305e+01
Coefficient B			-4.14561e+03
Coefficient C			-9.53240e+01
Reference			Collerson, Counsell, et al., 1965, 2
Temperature range, min.			477.36
Temperature range, max.			544.09

P_vap	26.55	kPa	477.36	Calculated Property
P_vap	32.65	kPa	484.77	Calculated Property
P_vap	39.83	kPa	492.19	Calculated Property
P_vap	48.24	kPa	499.60	Calculated Property
P_vap	58.02	kPa	507.02	Calculated Property
P_vap	69.34	kPa	514.43	Calculated Property
P_vap	82.34	kPa	521.85	Calculated Property
P_vap	97.22	kPa	529.26	Calculated Property
P_vap	114.15	kPa	536.68	Calculated Property
P_vap	133.31	kPa	544.09	Calculated Property
P_vap	[26.55; 133.31]	kPa	[477.36; 544.09]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.41305e+01
Coefficient B			-4.14561e+03
Coefficient C			-9.53240e+01
Reference			Collerson, Counsell, et al., 1965
Temperature range, min.			477.36
Temperature range, max.			544.09

P_vap	26.55	kPa	477.36	Calculated Property
P_vap	32.65	kPa	484.77	Calculated Property
P_vap	39.83	kPa	492.19	Calculated Property
P_vap	48.24	kPa	499.60	Calculated Property
P_vap	58.02	kPa	507.02	Calculated Property
P_vap	69.34	kPa	514.43	Calculated Property
P_vap	82.34	kPa	521.85	Calculated Property
P_vap	97.22	kPa	529.26	Calculated Property
P_vap	114.15	kPa	536.68	Calculated Property
P_vap	133.31	kPa	544.09	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[1066.32; 338.45]	kg/m³	[300.03; 766.80]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			8.87340e+01
Coefficient B			2.62180e-01
Coefficient C			7.66800e+02
Coefficient D			3.10330e-01
Temperature range, min.			300.03
Temperature range, max.			766.80

ρ_l	1066.32	kg/m³	300.03	Calculated Property
ρ_l	1023.29	kg/m³	351.89	Calculated Property
ρ_l	978.35	kg/m³	403.76	Calculated Property
ρ_l	931.02	kg/m³	455.62	Calculated Property
ρ_l	880.61	kg/m³	507.48	Calculated Property
ρ_l	826.04	kg/m³	559.35	Calculated Property
ρ_l	765.43	kg/m³	611.21	Calculated Property
ρ_l	695.02	kg/m³	663.07	Calculated Property
ρ_l	604.67	kg/m³	714.94	Calculated Property
ρ_l	338.45	kg/m³	766.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[300.15; 531.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.00057e-02
Coefficient B			-7.80000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			300.15
Temperature range, max.			531.15

γ	0.03	N/m	300.15	Calculated Property
γ	0.02	N/m	325.82	Calculated Property
γ	0.02	N/m	351.48	Calculated Property
γ	0.02	N/m	377.15	Calculated Property
γ	0.02	N/m	402.82	Calculated Property
γ	0.02	N/m	428.48	Calculated Property
γ	0.01	N/m	454.15	Calculated Property
γ	0.01	N/m	479.82	Calculated Property
γ	0.01	N/m	505.48	Calculated Property
γ	0.01	N/m	531.15	Calculated Property
γ	[0.04; 3.33e-06]	N/m	[293.15; 766.80]	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 γ in N/m, T in K
Coefficient A			7.43830e-02
Coefficient B			1.30180e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.67150e+02
Temperature range, min.			293.15
Temperature range, max.			766.80

γ	0.04	N/m	293.15	Calculated Property
γ	0.03	N/m	345.78	Calculated Property
γ	0.03	N/m	398.41	Calculated Property
γ	0.02	N/m	451.03	Calculated Property
γ	0.02	N/m	503.66	Calculated Property
γ	0.01	N/m	556.29	Calculated Property
γ	0.01	N/m	608.92	Calculated Property
γ	0.01	N/m	661.54	Calculated Property
γ	0.00	N/m	714.17	Calculated Property
γ	3.33e-06	N/m	766.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_gas	[0.02; 0.05]	W/m×K	[531.46; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ_gas in W/m×K, T in K
Coefficient A			1.46290e-04
Coefficient B			9.37700e-01
Coefficient C			7.45890e+02
Coefficient D			0.00000e+00
Temperature range, min.			531.46
Temperature range, max.			1000.00

λ_gas	0.02	W/m×K	531.46	Calculated Property
λ_gas	0.03	W/m×K	583.52	Calculated Property
λ_gas	0.03	W/m×K	635.58	Calculated Property
λ_gas	0.03	W/m×K	687.64	Calculated Property
λ_gas	0.04	W/m×K	739.70	Calculated Property
λ_gas	0.04	W/m×K	791.76	Calculated Property
λ_gas	0.04	W/m×K	843.82	Calculated Property
λ_gas	0.05	W/m×K	895.88	Calculated Property
λ_gas	0.05	W/m×K	947.94	Calculated Property
λ_gas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_liquid	[0.14; 0.11]	W/m×K	[300.03; 531.46]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ_liquid in W/m×K, T in K
Coefficient A			1.86860e-01
Coefficient B			-1.49530e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			300.03
Temperature range, max.			531.46

λ_liquid	0.14	W/m×K	300.03	Calculated Property
λ_liquid	0.14	W/m×K	325.74	Calculated Property
λ_liquid	0.13	W/m×K	351.46	Calculated Property
λ_liquid	0.13	W/m×K	377.17	Calculated Property
λ_liquid	0.13	W/m×K	402.89	Calculated Property
λ_liquid	0.12	W/m×K	428.60	Calculated Property
λ_liquid	0.12	W/m×K	454.32	Calculated Property
λ_liquid	0.12	W/m×K	480.03	Calculated Property
λ_liquid	0.11	W/m×K	505.75	Calculated Property
λ_liquid	0.11	W/m×K	531.46	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,1'-oxybis-.

Mixtures

Benzene, 1,1'-oxybis- + Biphenyl

Sources

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).
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
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.
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.
Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
Standard enthalpy of formation of diphenyl oxide
Benchmark properties of diphenyl oxide as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Determination of sublimation enthalpies of substituted benzophenones, fluorenes and diphenyl ethers by solution calorimetry approach
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
NCMS SOLV-DB
The Yaws Handbook of Vapor Pressure

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Chemical Properties of Benzene, 1,1'-oxybis- (CAS 101-84-8)