Chemical Properties of Methanethiol (CAS 63933-47-1)

InChI

InChI=1S/CH4S/c1-2/h2H,1H3

InChI Key

LSDPWZHWYPCBBB-UHFFFAOYSA-N

Formula

CH4S

SMILES

CS

Molecular Weight¹

48.11

CAS

63933-47-1

Other Names

• CH3SH
• Mercaptan methylique
• Mercaptomethane
• Methaanthiol
• Methanethiole
• Methanthiol
• Methvtiolo
• Methyl sulfhydrate
• Methyl thioalcohol
• Methylmercaptaan
• Metilmercaptano
• Rcra waste number U153
• Thiomethanol
• UN 1064
• methyl mercaptan

• ω : Acentric Factor.
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_{(+) ion} : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
• Δ_fH_{(+) ion,0K} : Enthalpy of formation of positive ion at 0K (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (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).
• 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_g : Gas Density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• 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	[0.1488; 0.1530]
ω	0.1488		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1500		ChemSep v8.3 pure component data Compiled value
ω	0.1530		KDB
μ	[1.30; 1.52]	debye
μ	1.52	debye	ChemSep v8.3 pure component data Compiled value
μ	1.30	debye	KDB
ΔfG°	[-9.92; -9.92]	kJ/mol
ΔfG°	-9.92	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-9.92	kJ/mol	KDB
ΔfH°gas	[-22.99; -22.60]	kJ/mol
ΔfH°gas	-22.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-22.99	kJ/mol	KDB
ΔfH°(+) ion	916.00	kJ/mol	NIST
ΔfH(+) ion,0K	925.00	kJ/mol	NIST
ΔfusH°	2.39	kJ/mol	Joback Calculated Property
ΔvapH°	25.17	kJ/mol	Relay (1.0) Calculated Property
IE	9.49	eV	Relay (1.0) Calculated Property
logPoct/wat	0.546		Crippen Calculated Property
McVol	41.300	ml/mol	McGowan Calculated Property
Pc	[7230.00; 7234.61]	kPa
Pc	7230.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value
Pc	7234.61	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	7230.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	7233.00	kPa	Air Liquide Gas Encyclopedia
Pc	7230.00	kPa	KDB
Ptriple	3.15e-03	kPa	ChemSep v8.3 pure component data Compiled value
Tboil	[279.11; 279.11]	K
Tboil	279.11	K	ChemSep v8.3 pure component data Compiled value
Tboil	279.11	K	Air Liquide Gas Encyclopedia
Tboil	279.11	K	KDB
Tc	[469.95; 470.00]	K
Tc	470.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value
Tc	470.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	470.00	K	ChemSep v8.3 pure component data Compiled value
Tc	469.95	K	Air Liquide Gas Encyclopedia
Tc	470.00	K	KDB
Tfus	[150.00; 151.15]	K
Tfus	151.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	150.18	K	ChemSep v8.3 pure component data Compiled value
Tfus	150.00	K	KDB
Ttriple	[150.17; 150.18]	K
Ttriple	150.17	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	150.18	K	ChemSep v8.3 pure component data Compiled value
UQi	1.68		ChemSep v8.3 pure component data Compiled value
URi	1.88		ChemSep v8.3 pure component data Compiled value
Vc	[0.145; 0.147]	m3/kmol
Vc	0.147	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value
Vc	0.145	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.145	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.145	m3/kmol	KDB
VCOSTALD	0.15	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.16		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2680000; 0.2720000]
Zc	0.2720000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value
Zc	0.2680000		ChemSep v8.3 pure component data Compiled value
Zc	0.2682700		KDB
Zra	[0.27; 0.28]
Zra	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value
Zra	0.28		KDB

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[24.54; 24.56]	kJ/mol	[279.10; 279.11]
ΔvapH	24.56	kJ/mol	279.10	KDB
ΔvapH	24.54	kJ/mol	279.11	Air Liquide Gas Encyclopedia
Pvap	[20.00; 200.00]	kPa	[243.19; 298.23]
Pvap	20.00	kPa	243.19	Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
Pvap	42.00	kPa	258.00	Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
Pvap	80.00	kPa	272.98	Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
Pvap	170.00	kPa	293.35	Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
Pvap	200.00	kPa	298.23	Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
ρg	[2.03; 2.12]	kg/m3	[279.11; 288.15]
ρg	2.12	kg/m3	279.11	Air Liquide Gas Encyclopedia
ρg	2.03	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[866.00; 886.00]	kg/m3	[279.11; 293.00]
ρl	886.00	kg/m3	279.11	Air Liquide Gas Encyclopedia
ρl	866.00	kg/m3	293.00	KDB
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[38.75; 107.64]	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			3.85350e+01
Coefficient B			-5.88350e+02
Coefficient C			4.32424e+00
Coefficient D			4.47820e-04
Coefficient E			-1.63630e-07
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	38.75	J/mol×K	100.00	Calculated Property
Cp,gas	46.91	J/mol×K	255.56	Calculated Property
Cp,gas	59.64	J/mol×K	411.11	Calculated Property
Cp,gas	71.23	J/mol×K	566.67	Calculated Property
Cp,gas	80.96	J/mol×K	722.22	Calculated Property
Cp,gas	88.99	J/mol×K	877.78	Calculated Property
Cp,gas	95.53	J/mol×K	1033.33	Calculated Property
Cp,gas	100.74	J/mol×K	1188.89	Calculated Property
Cp,gas	104.75	J/mol×K	1344.44	Calculated Property
Cp,gas	107.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[87.32; 90.47]	J/mol×K	[150.18; 298.15]	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			8.73180e+01
Coefficient B			-5.92220e+04
Coefficient C			5.43382e+02
Coefficient D			-1.65990e+00
Coefficient E			1.70200e-03
Temperature range, min.			150.18
Temperature range, max.			298.15
Cp,liquid	87.32	J/mol×K	150.18	Calculated Property
Cp,liquid	87.32	J/mol×K	166.62	Calculated Property
Cp,liquid	87.32	J/mol×K	183.06	Calculated Property
Cp,liquid	87.32	J/mol×K	199.50	Calculated Property
Cp,liquid	87.32	J/mol×K	215.94	Calculated Property
Cp,liquid	87.32	J/mol×K	232.39	Calculated Property
Cp,liquid	87.42	J/mol×K	248.83	Calculated Property
Cp,liquid	87.97	J/mol×K	265.27	Calculated Property
Cp,liquid	89.18	J/mol×K	281.71	Calculated Property
Cp,liquid	90.47	J/mol×K	298.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0020214; 0.0001631]	Pa×s	[150.18; 373.00]	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			-8.94700e+00
Coefficient B			6.07010e+02
Coefficient C			-2.64470e-01
Coefficient D			1.18070e-06
Coefficient E			2.00000e+00
Temperature range, min.			150.18
Temperature range, max.			373.00
η	0.0020214	Pa×s	150.18	Calculated Property
η	0.0011062	Pa×s	174.94	Calculated Property
η	0.0007023	Pa×s	199.70	Calculated Property
η	0.0004931	Pa×s	224.45	Calculated Property
η	0.0003717	Pa×s	249.21	Calculated Property
η	0.0002954	Pa×s	273.97	Calculated Property
η	0.0002443	Pa×s	298.73	Calculated Property
η	0.0002085	Pa×s	323.48	Calculated Property
η	0.0001825	Pa×s	348.24	Calculated Property
η	0.0001631	Pa×s	373.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[29.90; 2.27]	kJ/mol	[150.18; 469.95]	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			3.22137e+01
Coefficient B			-3.10105e-03
Coefficient C			6.57759e-01
Coefficient D			-2.49162e-02
Coefficient E			-3.40052e-01
Critical temperature, Tc (K)			4.70000e+02
Temperature range, min.			150.18
Temperature range, max.			469.95
ΔvapH	29.90	kJ/mol	150.18	Calculated Property
ΔvapH	28.67	kJ/mol	185.71	Calculated Property
ΔvapH	27.21	kJ/mol	221.24	Calculated Property
ΔvapH	25.55	kJ/mol	256.77	Calculated Property
ΔvapH	23.72	kJ/mol	292.30	Calculated Property
ΔvapH	21.76	kJ/mol	327.83	Calculated Property
ΔvapH	19.65	kJ/mol	363.36	Calculated Property
ΔvapH	17.30	kJ/mol	398.89	Calculated Property
ΔvapH	14.29	kJ/mol	434.42	Calculated Property
ΔvapH	2.27	kJ/mol	469.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4177.44]	kPa	[204.56; 429.95]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42712e+01
Coefficient B			-2.32325e+03
Coefficient C			-3.84210e+01
Temperature range, min.			204.56
Temperature range, max.			429.95
Pvap	1.33	kPa	204.56	Calculated Property
Pvap	8.32	kPa	229.60	Calculated Property
Pvap	34.01	kPa	254.65	Calculated Property
Pvap	103.75	kPa	279.69	Calculated Property
Pvap	256.59	kPa	304.73	Calculated Property
Pvap	543.11	kPa	329.78	Calculated Property
Pvap	1020.92	kPa	354.82	Calculated Property
Pvap	1749.38	kPa	379.86	Calculated Property
Pvap	2784.93	kPa	404.91	Calculated Property
Pvap	4177.44	kPa	429.95	Calculated Property
Pvap	[1.17e-03; 7569.07]	kPa	[150.18; 469.95]	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			1.08252e+02
Coefficient B			-6.30005e+03
Coefficient C			-1.46648e+01
Coefficient D			1.95265e-05
Coefficient E			2.00000e+00
Temperature range, min.			150.18
Temperature range, max.			469.95
Pvap	1.17e-03	kPa	150.18	Calculated Property
Pvap	0.20	kPa	185.71	Calculated Property
Pvap	4.73	kPa	221.24	Calculated Property
Pvap	38.12	kPa	256.77	Calculated Property
Pvap	164.61	kPa	292.30	Calculated Property
Pvap	486.63	kPa	327.83	Calculated Property
Pvap	1138.15	kPa	363.36	Calculated Property
Pvap	2303.65	kPa	398.89	Calculated Property
Pvap	4276.27	kPa	434.42	Calculated Property
Pvap	7569.07	kPa	469.95	Calculated Property
Pvap	[1.37e-03; 7232.87]	kPa	[150.18; 470.00]	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			9.18684e+01
Coefficient B			-5.80626e+03
Coefficient C			-1.19968e+01
Coefficient D			1.44187e-05
Coefficient E			0.00000e+00
Temperature range, min.			150.18
Temperature range, max.			470.00
Pvap	1.37e-03	kPa	150.18	Calculated Property
Pvap	0.21	kPa	185.72	Calculated Property
Pvap	4.74	kPa	221.25	Calculated Property
Pvap	38.34	kPa	256.79	Calculated Property
Pvap	167.61	kPa	292.32	Calculated Property
Pvap	500.66	kPa	327.86	Calculated Property
Pvap	1173.04	kPa	363.39	Calculated Property
Pvap	2349.47	kPa	398.93	Calculated Property
Pvap	4254.38	kPa	434.46	Calculated Property
Pvap	7232.87	kPa	470.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1037.31; 543.07]	kg/m3	[150.18; 453.12]	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			9.40020e+01
Coefficient B			2.81710e-01
Coefficient C			4.70000e+02
Coefficient D			2.87370e-01
Temperature range, min.			150.18
Temperature range, max.			453.12
ρl	1037.31	kg/m3	150.18	Calculated Property
ρl	1000.96	kg/m3	183.84	Calculated Property
ρl	962.87	kg/m3	217.50	Calculated Property
ρl	922.63	kg/m3	251.16	Calculated Property
ρl	879.69	kg/m3	284.82	Calculated Property
ρl	833.19	kg/m3	318.48	Calculated Property
ρl	781.75	kg/m3	352.14	Calculated Property
ρl	722.78	kg/m3	385.80	Calculated Property
ρl	650.44	kg/m3	419.46	Calculated Property
ρl	543.07	kg/m3	453.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.03]	N/m	[150.15; 279.15]	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			7.44162e-02
Coefficient B			-1.69600e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			150.15
Temperature range, max.			279.15
γ	0.05	N/m	150.15	Calculated Property
γ	0.05	N/m	164.48	Calculated Property
γ	0.04	N/m	178.82	Calculated Property
γ	0.04	N/m	193.15	Calculated Property
γ	0.04	N/m	207.48	Calculated Property
γ	0.04	N/m	221.82	Calculated Property
γ	0.03	N/m	236.15	Calculated Property
γ	0.03	N/m	250.48	Calculated Property
γ	0.03	N/m	264.82	Calculated Property
γ	0.03	N/m	279.15	Calculated Property
γ	[0.05; 1.28e-05]	N/m	[150.18; 467.39]	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			-1.34600e-02
Coefficient B			4.14230e+01
Coefficient C			-3.01120e+00
Coefficient D			1.36070e-03
Coefficient E			-9.24900e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 469.95 K.
Temperature range, min.			150.18
Temperature range, max.			467.39
γ	0.05	N/m	150.18	Calculated Property
γ	0.04	N/m	185.43	Calculated Property
γ	0.04	N/m	220.67	Calculated Property
γ	0.03	N/m	255.92	Calculated Property
γ	0.03	N/m	291.16	Calculated Property
γ	0.02	N/m	326.41	Calculated Property
γ	0.01	N/m	361.65	Calculated Property
γ	0.01	N/m	396.90	Calculated Property
γ	0.00	N/m	432.15	Calculated Property
γ	1.28e-05	N/m	467.39	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[150.18; 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			2.46890e-05
Coefficient B			1.17020e+00
Coefficient C			4.71840e+00
Coefficient D			3.54660e+04
Temperature range, min.			150.18
Temperature range, max.			1000.00
λgas	0.00	W/m×K	150.18	Calculated Property
λgas	0.01	W/m×K	244.60	Calculated Property
λgas	0.02	W/m×K	339.03	Calculated Property
λgas	0.03	W/m×K	433.45	Calculated Property
λgas	0.03	W/m×K	527.88	Calculated Property
λgas	0.04	W/m×K	622.30	Calculated Property
λgas	0.05	W/m×K	716.73	Calculated Property
λgas	0.06	W/m×K	811.15	Calculated Property
λgas	0.07	W/m×K	905.58	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.20; 0.15]	W/m×K	[150.18; 279.11]	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			-1.12420e-02
Coefficient B			-1.14240e+01
Coefficient C			-1.17010e+00
Coefficient D			-1.77290e-03
Coefficient E			-1.20430e-06
Temperature range, min.			150.18
Temperature range, max.			279.11
λliquid	0.20	W/m×K	150.18	Calculated Property
λliquid	0.20	W/m×K	164.51	Calculated Property
λliquid	0.19	W/m×K	178.83	Calculated Property
λliquid	0.19	W/m×K	193.16	Calculated Property
λliquid	0.18	W/m×K	207.48	Calculated Property
λliquid	0.18	W/m×K	221.81	Calculated Property
λliquid	0.17	W/m×K	236.13	Calculated Property
λliquid	0.17	W/m×K	250.46	Calculated Property
λliquid	0.16	W/m×K	264.78	Calculated Property
λliquid	0.15	W/m×K	279.11	Calculated Property

Similar Compounds

Find more compounds similar to Methanethiol.

Mixtures

• Methanethiol + Methane
• Methanethiol + Water
• Methanethiol + Nitrogen
• Methanethiol + Carbon dioxide

Sources

• KDB Vapor Pressure Data
• Air Liquide Gas Encyclopedia
• 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.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 8. Organic Sulfur, Silicon, and Tin Compounds (C + H + S, Si, and Sn). J. Chem. Eng. Data 2001, 46, 480-485.
• 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.
• 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.
• 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
• Crippen Method
• Gas liquid partition coefficients and Henry s law constants of methyl mercaptan in aqueous solutions of Fe(II) CDTA chelate complex
• Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
• Phase Equilibria of Three Binary Mixtures: Methanethiol + Methane, Methanethiol + Nitrogen, and Methanethiol + Carbon Dioxide
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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