Chemical Properties of 1,4-Benzenedicarboxylic acid, dimethyl ester (CAS 120-61-6)

InChI

InChI=1S/C10H10O4/c1-13-9(11)7-3-5-8(6-4-7)10(12)14-2/h3-6H,1-2H3

InChI Key

WOZVHXUHUFLZGK-UHFFFAOYSA-N

Formula

C10H10O4

SMILES

COC(=O)c1ccc(C(=O)OC)cc1

Molecular Weight¹

194.18

CAS

120-61-6

Other Names

• 1,4-Benzenedicarboxylic acid dimethyl ester
• 1,4-Benzenedicarboxylic acid, 1,4-dimethyl ester
• DMT
• Dimethyl ester of 1,4-benzenedicarboxylic acid
• Dimethyl p-benzenedicarboxylate
• Dimethyl p-phthalate
• Dimethyl terphthalate
• Dimethylester kyseliny isoftalove
• Dimethylester kyseliny tereftalove
• Methyl 4-(carbomethoxy)benzoate
• Methyl p-(methoxycarbonyl)benzoate
• NCI-C50055
• NSC 3503
• Terephthalate, dimethyl
• Terephthalic acid, dimethyl ester
• dimethyl 1,4-benzenedicarboxylate
• dimethyl benzene-1,4-dicarboxylate
• dimethyl terephthalate

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (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).
• EA : Electron affinity (eV).
• 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_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_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (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).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6371		ChemSep v8.3 pure component data Compiled value
PAff	843.20	kJ/mol	NIST
BasG	812.30	kJ/mol	NIST
ΔcH°solid	-4631.66 ± 0.88	kJ/mol	NIST
μ	2.19	debye	ChemSep v8.3 pure component data Compiled value
EA	[0.64; 0.82]	eV
EA	0.82 ± 0.09	eV	NIST
EA	0.82 ± 0.09	eV	NIST
EA	0.64	eV	NIST
ΔfG°	-474.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-637.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°solid	[-732.60; -710.00]	kJ/mol
ΔfH°solid	-710.00	kJ/mol	NIST
ΔfH°solid	-732.60 ± 1.00	kJ/mol	NIST
ΔfusH°	[33.01; 35.50]	kJ/mol
ΔfusH°	35.50	kJ/mol	New aspects of relationship between the enthalpies of fusion of aromatic compounds at the melting temperature and the enthalpies of solution in benzene at 298.15 K. Part II
ΔfusH°	33.01	kJ/mol	Thermal analysis of phase change materials in the temperature range 120.150 .C
ΔsubH°	[104.60; 104.60]	kJ/mol
ΔsubH°	104.60 ± 0.30	kJ/mol	NIST
ΔsubH°	104.60 ± 0.30	kJ/mol	NIST
ΔvapH°	83.31	kJ/mol	Relay (1.0) Calculated Property
IE	9.78 ± 0.03	eV	NIST
log10WS	-3.72		Aq. Solubility Prediction
logPoct/wat	1.260		Crippen Calculated Property
McVol	142.880	ml/mol	McGowan Calculated Property
Pc	2780.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	1.26	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[1461.00; 1512.00]
Inp	1461.00		NIST
Inp	1470.00		NIST
Inp	1480.00		NIST
Inp	1492.00		NIST
Inp	1468.00		NIST
Inp	1475.00		NIST
Inp	1469.00		NIST
Inp	Outlier 1512.00		NIST
Inp	1468.00		NIST
Inp	1473.00		NIST
Inp	1475.00		NIST
Inp	1475.00		NIST
Inp	Outlier 1512.00		NIST
Inp	1469.00		NIST
Inp	1475.00		NIST
Tboil	555.15	K	ChemSep v8.3 pure component data Compiled value
Tc	[772.00; 779.00]	K
Tc	779.00	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	772.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[413.00; 415.20]	K
Tfus	413.80	K	ChemSep v8.3 pure component data Compiled value
Tfus	414.40	K	Aq. Solubility Prediction
Tfus	Outlier 415.20 ± 0.20	K	NIST
Tfus	413.80 ± 0.01	K	NIST
Tfus	413.80 ± 0.20	K	NIST
Tfus	413.00 ± 4.00	K	NIST
Tfus	413.00 ± 1.50	K	NIST
Tfus	413.80 ± 0.01	K	NIST
Tfus	413.80 ± 0.20	K	NIST
Ttriple	[413.80; 413.88]	K
Ttriple	413.88	K	Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
Ttriple	413.80	K	ChemSep v8.3 pure component data Compiled value
UQi	5.30		ChemSep v8.3 pure component data Compiled value
URi	6.66		ChemSep v8.3 pure component data Compiled value
Vc	0.529	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2290000		ChemSep v8.3 pure component data Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,solid	[261.10; 276.10]	J/mol×K	[298.15; 353.00]
Cp,solid	261.10	J/mol×K	298.15	NIST
Cp,solid	276.10	J/mol×K	353.00	NIST
ΔfusH	[31.63; 32.10]	kJ/mol	[413.79; 415.40]
ΔfusH	31.63	kJ/mol	413.79	NIST
ΔfusH	31.63	kJ/mol	413.79	NIST
ΔfusH	32.10	kJ/mol	413.80	NIST
ΔfusH	32.09	kJ/mol	413.80	NIST
ΔfusH	32.10	kJ/mol	413.80	NIST
ΔfusH	32.00	kJ/mol	415.40	NIST
ΔsubH	[88.30; 103.80]	kJ/mol	[320.50; 393.00]
ΔsubH	103.80 ± 0.30	kJ/mol	320.50	NIST
ΔsubH	94.40	kJ/mol	393.00	NIST
ΔsubH	88.30	kJ/mol	393.00	NIST
ΔvapH	62.00	kJ/mol	468.00	NIST
ΔfusS	[76.44; 77.60]	J/mol×K	[413.79; 415.40]
ΔfusS	76.44	J/mol×K	413.79	NIST
ΔfusS	76.44	J/mol×K	413.79	NIST
ΔfusS	77.60	J/mol×K	413.80	NIST
ΔfusS	77.60	J/mol×K	413.80	NIST
ΔfusS	77.00	J/mol×K	415.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[152.45; 412.86]	J/mol×K	[273.00; 1000.15]	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			9.55460e+01
Coefficient B			-9.44260e+02
Coefficient C			8.15124e+00
Coefficient D			-2.73730e-03
Coefficient E			1.29010e-06
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			273.00
Temperature range, max.			1000.15
Cp,gas	152.45	J/mol×K	273.00	Calculated Property
Cp,gas	202.81	J/mol×K	353.79	Calculated Property
Cp,gas	248.87	J/mol×K	434.59	Calculated Property
Cp,gas	286.31	J/mol×K	515.38	Calculated Property
Cp,gas	315.63	J/mol×K	596.18	Calculated Property
Cp,gas	338.92	J/mol×K	676.97	Calculated Property
Cp,gas	358.42	J/mol×K	757.77	Calculated Property
Cp,gas	376.16	J/mol×K	838.56	Calculated Property
Cp,gas	393.82	J/mol×K	919.36	Calculated Property
Cp,gas	412.86	J/mol×K	1000.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[373.04; 391.41]	J/mol×K	[423.15; 466.35]	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			3.06140e+02
Coefficient B			1.15180e+03
Coefficient C			-5.08986e+00
Coefficient D			1.92260e-02
Coefficient E			-8.73710e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			423.15
Temperature range, max.			466.35
Cp,liquid	373.04	J/mol×K	423.15	Calculated Property
Cp,liquid	374.80	J/mol×K	427.95	Calculated Property
Cp,liquid	376.64	J/mol×K	432.75	Calculated Property
Cp,liquid	378.54	J/mol×K	437.55	Calculated Property
Cp,liquid	380.50	J/mol×K	442.35	Calculated Property
Cp,liquid	382.54	J/mol×K	447.15	Calculated Property
Cp,liquid	384.65	J/mol×K	451.95	Calculated Property
Cp,liquid	386.83	J/mol×K	456.75	Calculated Property
Cp,liquid	389.08	J/mol×K	461.55	Calculated Property
Cp,liquid	391.41	J/mol×K	466.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0010688; 0.0003157]	Pa×s	[413.80; 561.15]	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			-9.60270e+00
Coefficient B			1.84580e+03
Coefficient C			-2.89910e-01
Coefficient D			2.78670e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			413.80
Temperature range, max.			561.15
η	0.0010688	Pa×s	413.80	Calculated Property
η	0.0008953	Pa×s	430.17	Calculated Property
η	0.0007598	Pa×s	446.54	Calculated Property
η	0.0006523	Pa×s	462.92	Calculated Property
η	0.0005660	Pa×s	479.29	Calculated Property
η	0.0004957	Pa×s	495.66	Calculated Property
η	0.0004380	Pa×s	512.03	Calculated Property
η	0.0003900	Pa×s	528.41	Calculated Property
η	0.0003497	Pa×s	544.78	Calculated Property
η	0.0003157	Pa×s	561.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[60.92; 26.45]	kJ/mol	[413.80; 753.15]	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			4.92727e+01
Coefficient B			-8.26644e-01
Coefficient C			8.40569e-01
Coefficient D			5.47723e-01
Coefficient E			-3.73819e-01
Critical temperature, Tc (K)			7.72000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			413.80
Temperature range, max.			753.15
ΔvapH	60.92	kJ/mol	413.80	Calculated Property
ΔvapH	59.92	kJ/mol	451.51	Calculated Property
ΔvapH	58.40	kJ/mol	489.21	Calculated Property
ΔvapH	56.33	kJ/mol	526.92	Calculated Property
ΔvapH	53.68	kJ/mol	564.62	Calculated Property
ΔvapH	50.40	kJ/mol	602.33	Calculated Property
ΔvapH	46.43	kJ/mol	640.03	Calculated Property
ΔvapH	41.60	kJ/mol	677.74	Calculated Property
ΔvapH	35.52	kJ/mol	715.44	Calculated Property
ΔvapH	26.45	kJ/mol	753.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[430.99; 587.72]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50856e+01
Coefficient B			-4.51226e+03
Coefficient C			-1.26067e+02
Temperature range, min.			430.99
Temperature range, max.			587.72
Pvap	1.33	kPa	430.99	Calculated Property
Pvap	2.97	kPa	448.40	Calculated Property
Pvap	6.08	kPa	465.82	Calculated Property
Pvap	11.61	kPa	483.23	Calculated Property
Pvap	20.89	kPa	500.65	Calculated Property
Pvap	35.68	kPa	518.06	Calculated Property
Pvap	58.22	kPa	535.48	Calculated Property
Pvap	91.27	kPa	552.89	Calculated Property
Pvap	138.14	kPa	570.31	Calculated Property
Pvap	202.64	kPa	587.72	Calculated Property
Pvap	[1.24; 1271.54]	kPa	[413.80; 772.00]	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			8.04443e+01
Coefficient B			-1.10618e+04
Coefficient C			-8.88269e+00
Coefficient D			1.56669e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			413.80
Temperature range, max.			772.00
Pvap	1.24	kPa	413.80	Calculated Property
Pvap	5.77	kPa	453.60	Calculated Property
Pvap	19.66	kPa	493.40	Calculated Property
Pvap	52.94	kPa	533.20	Calculated Property
Pvap	118.83	kPa	573.00	Calculated Property
Pvap	230.99	kPa	612.80	Calculated Property
Pvap	400.30	kPa	652.60	Calculated Property
Pvap	632.12	kPa	692.40	Calculated Property
Pvap	925.11	kPa	732.20	Calculated Property
Pvap	1271.54	kPa	772.00	Calculated Property
Pvap	[0.82; 2774.43]	kPa	[403.80; 772.00]	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			5.91810e+01
Coefficient B			-9.27175e+03
Coefficient C			-6.14065e+00
Coefficient D			2.66169e-06
Coefficient E			0.00000e+00
Temperature range, min.			403.80
Temperature range, max.			772.00
Pvap	0.82	kPa	403.80	Calculated Property
Pvap	4.12	kPa	444.71	Calculated Property
Pvap	15.39	kPa	485.62	Calculated Property
Pvap	46.09	kPa	526.53	Calculated Property
Pvap	116.73	kPa	567.44	Calculated Property
Pvap	259.61	kPa	608.36	Calculated Property
Pvap	521.55	kPa	649.27	Calculated Property
Pvap	966.72	kPa	690.18	Calculated Property
Pvap	1680.44	kPa	731.09	Calculated Property
Pvap	2774.43	kPa	772.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1075.43; 604.11]	kg/m3	[413.80; 753.15]	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			9.87697e+01
Coefficient B			2.68950e-01
Coefficient C			7.72000e+02
Coefficient D			2.61330e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			413.80
Temperature range, max.			753.15
ρl	1075.43	kg/m3	413.80	Calculated Property
ρl	1042.83	kg/m3	451.51	Calculated Property
ρl	1008.39	kg/m3	489.21	Calculated Property
ρl	971.69	kg/m3	526.92	Calculated Property
ρl	932.13	kg/m3	564.62	Calculated Property
ρl	888.81	kg/m3	602.33	Calculated Property
ρl	840.25	kg/m3	640.03	Calculated Property
ρl	783.70	kg/m3	677.74	Calculated Property
ρl	712.87	kg/m3	715.44	Calculated Property
ρl	604.11	kg/m3	753.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[413.80; 753.15]	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			-5.89130e-02
Coefficient B			-2.67140e+01
Coefficient C			-1.92820e+00
Coefficient D			-1.18870e-03
Coefficient E			8.16720e-08
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			413.80
Temperature range, max.			753.15
γ	0.03	N/m	413.80	Calculated Property
γ	0.02	N/m	451.51	Calculated Property
γ	0.02	N/m	489.21	Calculated Property
γ	0.02	N/m	526.92	Calculated Property
γ	0.01	N/m	564.62	Calculated Property
γ	0.01	N/m	602.33	Calculated Property
γ	0.01	N/m	640.03	Calculated Property
γ	0.01	N/m	677.74	Calculated Property
γ	0.00	N/m	715.44	Calculated Property
γ	0.00	N/m	753.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.05]	W/m×K	[274.00; 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			-2.19380e+04
Coefficient B			3.22020e-01
Coefficient C			-4.32750e+09
Coefficient D			-1.52650e+11
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			274.00
Temperature range, max.			1000.00
λgas	0.01	W/m×K	274.00	Calculated Property
λgas	0.01	W/m×K	354.67	Calculated Property
λgas	0.01	W/m×K	435.33	Calculated Property
λgas	0.02	W/m×K	516.00	Calculated Property
λgas	0.02	W/m×K	596.67	Calculated Property
λgas	0.03	W/m×K	677.33	Calculated Property
λgas	0.03	W/m×K	758.00	Calculated Property
λgas	0.04	W/m×K	838.67	Calculated Property
λgas	0.04	W/m×K	919.33	Calculated Property
λgas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.10]	W/m×K	[413.80; 561.15]	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			-1.52060e-02
Coefficient B			-2.75630e+02
Coefficient C			5.85690e-02
Coefficient D			-3.50780e-03
Coefficient E			7.37450e-07
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			413.80
Temperature range, max.			561.15
λliquid	0.13	W/m×K	413.80	Calculated Property
λliquid	0.13	W/m×K	430.17	Calculated Property
λliquid	0.12	W/m×K	446.54	Calculated Property
λliquid	0.12	W/m×K	462.92	Calculated Property
λliquid	0.12	W/m×K	479.29	Calculated Property
λliquid	0.11	W/m×K	495.66	Calculated Property
λliquid	0.11	W/m×K	512.03	Calculated Property
λliquid	0.11	W/m×K	528.41	Calculated Property
λliquid	0.10	W/m×K	544.78	Calculated Property
λliquid	0.10	W/m×K	561.15	Calculated Property

Similar Compounds

Find more compounds similar to 1,4-Benzenedicarboxylic acid, dimethyl ester.

Mixtures

• 1,4-Benzenedicarboxylic acid, dimethyl ester + Methyl Alcohol
• Ethanol + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 1-Propanol + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 2-Propanol + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 1-Butanol + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 1,4-Benzenedicarboxylic acid, dimethyl ester + Ethyl Acetate
• 1,4-Benzenedicarboxylic acid, dimethyl ester + Isopropyl acetate
• 1,4-Benzenedicarboxylic acid, dimethyl ester + Acetic acid, propyl ester
• Acetic acid, butyl ester + 1,4-Benzenedicarboxylic acid, dimethyl ester
• Acetic acid, pentyl ester + 1,4-Benzenedicarboxylic acid, dimethyl ester
• Methyl propionate + 1,4-Benzenedicarboxylic acid, dimethyl ester
• Acetone + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 2-Butanone + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 1,4-Benzenedicarboxylic acid, dimethyl ester + Cyclohexanone
• Acetonitrile + 1,4-Benzenedicarboxylic acid, dimethyl ester
• Trichloromethane + 1,4-Benzenedicarboxylic acid, dimethyl ester
• 1-Propanol, 2-methyl- + 1,4-Benzenedicarboxylic acid, dimethyl ester

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• 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
• New aspects of relationship between the enthalpies of fusion of aromatic compounds at the melting temperature and the enthalpies of solution in benzene at 298.15 K. Part II
• Thermal analysis of phase change materials in the temperature range 120.150 .C
• New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
• Enthalpies of fusion and enthalpies of solvation of aromatic hydrocarbons derivatives: Estimation of sublimation enthalpies at 298.15K
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Joback Method
• KDB
• Aqueous Solubility Prediction 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.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.