Chemical Properties of Dibenzothiophene (CAS 132-65-0)

InChI

InChI=1S/C12H8S/c1-3-7-11-9(5-1)10-6-2-4-8-12(10)13-11/h1-8H

InChI Key

IYYZUPMFVPLQIF-UHFFFAOYSA-N

Formula

C12H8S

SMILES

c1ccc2c(c1)sc1ccccc12

Molecular Weight¹

184.26

CAS

132-65-0

Other Names

• 2,2'-Biphenylylene sulfide
• 9-Thiafluorene
• Dibenzo[b,d]thiophene
• Diphenylene sulfide
• [1,1'-Biphenyl]-2,2'-diyl sulfide
• «alpha»-Thiafluorene
• «alpha»-Thiafluorene

• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• 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 a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation 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_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°solid	[-6587.70; -6571.60]	kJ/mol
ΔcH°solid	-6571.60 ± 4.40	kJ/mol	NIST
ΔcH°solid	-6587.70 ± 1.30	kJ/mol	NIST
ΔfH°gas	[189.30; 213.20]	kJ/mol
ΔfH°gas	213.20 ± 0.70	kJ/mol	NIST
ΔfH°gas	189.30 ± 4.50	kJ/mol	NIST
ΔfH°gas	205.40	kJ/mol	NIST
ΔfH°solid	[104.20; 120.30]	kJ/mol
ΔfH°solid	104.20 ± 4.50	kJ/mol	NIST
ΔfH°solid	120.30 ± 1.50	kJ/mol	NIST
ΔsubH°	[85.09; 97.50]	kJ/mol
ΔsubH°	93.20 ± 0.50	kJ/mol	NIST
ΔsubH°	93.30	kJ/mol	NIST
ΔsubH°	85.10 ± 0.40	kJ/mol	NIST
ΔsubH°	85.09 ± 0.35	kJ/mol	NIST
ΔsubH°	85.10	kJ/mol	NIST
ΔsubH°	97.50	kJ/mol	NIST
ΔvapH°	78.30 ± 1.10	kJ/mol	NIST
IE	[7.90; 8.44]	eV
IE	8.44	eV	NIST
IE	8.34	eV	NIST
IE	8.23	eV	NIST
IE	7.90 ± 0.03	eV	NIST
IE	8.14	eV	NIST
IE	7.93	eV	NIST
IE	8.01	eV	NIST
log10WS	[-4.62; -4.38]
log10WS	-4.62		Aq. Sol...
log10WS	-4.38		Estimat...
logPoct/wat	4.054		Crippen Calculated Property
McVol	137.910	ml/mol	McGowan Calculated Property
Inp	[293.59; 1780.00]
Inp	1717.00		NIST
Inp	1739.80		NIST
Inp	1741.90		NIST
Inp	1728.00		NIST
Inp	1733.00		NIST
Inp	1742.00		NIST
Inp	1724.00		NIST
Inp	1722.00		NIST
Inp	1719.00		NIST
Inp	1719.00		NIST
Inp	1764.00		NIST
Inp	1774.00		NIST
Inp	1774.00		NIST
Inp	1776.00		NIST
Inp	1780.00		NIST
Inp	1728.00		NIST
Inp	1721.00		NIST
Inp	1766.00		NIST
Inp	1768.00		NIST
Inp	295.47		NIST
Inp	295.99		NIST
Inp	296.06		NIST
Inp	295.59		NIST
Inp	295.59		NIST
Inp	295.73		NIST
Inp	295.85		NIST
Inp	295.60		NIST
Inp	295.60		NIST
Inp	296.01		NIST
Inp	295.77		NIST
Inp	295.78		NIST
Inp	295.96		NIST
Inp	296.30		NIST
Inp	295.90		NIST
Inp	295.95		NIST
Inp	295.40		NIST
Inp	295.59		NIST
Inp	295.90		NIST
Inp	296.03		NIST
Inp	294.74		NIST
Inp	295.31		NIST
Inp	296.00		NIST
Inp	295.39		NIST
Inp	296.01		NIST
Inp	295.81		NIST
Inp	296.00		NIST
Inp	295.95		NIST
Inp	295.59		NIST
Inp	295.95		NIST
Inp	295.70		NIST
Inp	295.70		NIST
Inp	294.65		NIST
Inp	293.59		NIST
Inp	295.70		NIST
Inp	295.28		NIST
Inp	295.24		NIST
Inp	295.20		NIST
Inp	295.80		NIST
Inp	295.90		NIST
Inp	295.90		NIST
Inp	294.90		NIST
Inp	295.90		NIST
Inp	295.81		NIST
Inp	1728.00		NIST
Inp	295.47		NIST
Inp	295.73		NIST
Inp	295.77		NIST
Inp	295.95		NIST
Inp	294.74		NIST
Inp	295.81		NIST
Inp	1741.90		NIST
I	295.17		NIST
S°solid,1 bar	204.20	J/mol×K	NIST
Tboil	605.70	K	NIST
Tfus	[371.00; 373.15]	K
Tfus	373.15	K	Thermod...
Tfus	373.15	K	Thermod...
Tfus	371.90 ± 0.30	K	NIST
Tfus	371.40 ± 0.10	K	NIST
Tfus	371.00 ± 0.70	K	NIST
Tfus	372.40 ± 0.30	K	NIST
Tfus	373.00 ± 2.00	K	NIST
Tfus	372.00 ± 2.00	K	NIST
Tfus	372.00 ± 2.00	K	NIST
Ttriple	371.82 ± 0.00	K	NIST

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,solid	[194.60; 198.30]	J/mol×K	[298.15; 298.15]
Cp,solid	198.30	J/mol×K	298.15	NIST
Cp,solid	194.60	J/mol×K	298.15	NIST
ΔfusH	[21.58; 21.71]	kJ/mol	[371.00; 373.20]
ΔfusH	21.58	kJ/mol	371.00	NIST
ΔfusH	21.58	kJ/mol	371.00	NIST
ΔfusH	21.58	kJ/mol	371.00	NIST
ΔfusH	21.60	kJ/mol	371.80	NIST
ΔfusH	21.71	kJ/mol	371.82	NIST
ΔfusH	21.60	kJ/mol	373.20	NIST
ΔfusH	21.60	kJ/mol	373.20	NIST
ΔsubH	[90.70; 91.20]	kJ/mol	[325.50; 348.00]
ΔsubH	91.20	kJ/mol	325.50	NIST
ΔsubH	90.70	kJ/mol	348.00	NIST
ΔvapH	[51.80; 69.50]	kJ/mol	[380.00; 630.00]
ΔvapH	69.50 ± 0.30	kJ/mol	380.00	NIST
ΔvapH	69.40	kJ/mol	388.00	NIST
ΔvapH	65.60	kJ/mol	398.50	NIST
ΔvapH	66.80 ± 0.30	kJ/mol	420.00	NIST
ΔvapH	64.30 ± 0.30	kJ/mol	460.00	NIST
ΔvapH	60.10	kJ/mol	479.50	NIST
ΔvapH	61.80 ± 0.30	kJ/mol	500.00	NIST
ΔvapH	63.40	kJ/mol	516.00	NIST
ΔvapH	58.70 ± 0.10	kJ/mol	518.50	NIST
ΔvapH	51.80 ± 0.40	kJ/mol	518.50	NIST
ΔvapH	55.40 ± 0.30	kJ/mol	518.50	NIST
ΔvapH	68.00 ± 0.10	kJ/mol	518.50	NIST
ΔvapH	61.80 ± 0.10	kJ/mol	518.50	NIST
ΔvapH	64.90 ± 0.10	kJ/mol	518.50	NIST
ΔvapH	59.30 ± 0.30	kJ/mol	540.00	NIST
ΔvapH	56.80 ± 0.30	kJ/mol	580.00	NIST
ΔvapH	56.90	kJ/mol	590.00	NIST
ΔvapH	55.30	kJ/mol	610.00	NIST
ΔvapH	54.00 ± 0.30	kJ/mol	620.00	NIST
ΔvapH	53.60	kJ/mol	630.00	NIST
ΔfusS	[58.17; 58.38]	J/mol×K	[371.00; 371.82]
ΔfusS	58.17	J/mol×K	371.00	NIST
ΔfusS	58.38	J/mol×K	371.82	NIST

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.47; 202.66]	kPa	[424.00; 640.91]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.73523e+01
Coefficient B			-7.78795e+03
Coefficient C			5.89000e+00
Temperature range, min.			424.00
Temperature range, max.			640.91
Pvap	0.47	kPa	424.00	Calculated Property
Pvap	1.22	kPa	448.10	Calculated Property
Pvap	2.89	kPa	472.20	Calculated Property
Pvap	6.32	kPa	496.30	Calculated Property
Pvap	12.87	kPa	520.40	Calculated Property
Pvap	24.59	kPa	544.51	Calculated Property
Pvap	44.53	kPa	568.61	Calculated Property
Pvap	76.86	kPa	592.71	Calculated Property
Pvap	127.17	kPa	616.81	Calculated Property
Pvap	202.66	kPa	640.91	Calculated Property

Similar Compounds

Find more compounds similar to Dibenzothiophene.

Mixtures

• Acetonitrile + Dibenzothiophene + Methyl Alcohol
• Dibenzothiophene + Methyl Alcohol
• Acetonitrile + Dibenzothiophene
• Pentane + Dibenzothiophene
• n-Hexane + Dibenzothiophene
• Cyclohexane + Dibenzothiophene
• Heptane + Dibenzothiophene
• Octane + Dibenzothiophene
• Pentane, 2,2,4-trimethyl- + Dibenzothiophene
• Nonane + Dibenzothiophene
• Decane + Dibenzothiophene
• Undecane + Dibenzothiophene
• Dodecane + Dibenzothiophene
• Ethanol + Dibenzothiophene
• Isopropyl Alcohol + Dibenzothiophene
• 1-Butanol + Dibenzothiophene
• Formic acid + Dibenzothiophene
• Tetradecane + Dibenzothiophene
• Hexadecane + Dibenzothiophene
• Formic acid + 1-Butanol + Dibenzothiophene

Find more mixtures with Dibenzothiophene.

Sources

• Crippen Method
• Feasibility of phosphonium-based ionic liquids as solvents for extractive desulfurization of liquid fuels
• Thermodynamic analysis for determination of solid - liquid equilibrium of dibenzothiophene in a binary solvent of formic acid and butan-1-ol between (278.15 and 333.15) K
• Measurements and prediction of ternary liquid-liquid equilibria for mixtures of IL + sulfur compound + hexadecane
• Revisiting dibenzothiophene thermochemical data: Experimental and computational studies
• Thermodynamic models for determination of the solubility of dibenzothiophene in (methanol + acetonitrile) binary solvent mixtures
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Solubility of Dibenzothiophene in Sub- and Supercritical Propane
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Liquid Liquid Equilibrium in N-Methyl-2-hydroxyethylammonium Acetate, Butanoate, or Hexanoate Ionic Liquids + Dibenzothiophene + n-Dodecane Systems at 298.2 K and Atmospheric Pressure
• Thermodynamic Models for Determination of the Solubility of Dibenzothiophene in Different Solvents at Temperatures from (278.15 to 328.15) K
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Infinite Dilution Binary Diffusion Coefficients of Hydrotreating Compounds in Tetradecane in the Temperature Range from (310 to 475) K
• 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.