Chemical Properties of Hydrogen sulfide (CAS 7783-06-4)

InChI

InChI=1S/H2S/h1H2

InChI Key

RWSOTUBLDIXVET-UHFFFAOYSA-N

Formula

H2S

SMILES

S

Molecular Weight¹

34.08

CAS

7783-06-4

Other Names

• Acide sulfhydrique
• DIHYDROGEN MONOSULFIDE
• Dihydrogen sulfide
• H2S
• HYDROSULFURIC ACID
• Hepatic acid
• Hepatic gas
• Hydrogen monosulfide
• Hydrogen sulfide (H2S)
• Hydrogen sulphide
• Hydrogene sulfure
• Idrogeno solforato
• Rcra waste number U135
• SULFUR HYDRIDE
• Schwefelwasserstoff
• Sewer gas
• Siarkowodor
• Stink damp
• Sulfureted hydrogen
• Sulfuretted hydrogen
• UN 1053
• Zwavelwaterstof

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• S°_{gas,1 bar} : Molar entropy at standard conditions (1 bar) (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• 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	0.0810		KDB
PAff	705.00	kJ/mol	NIST
BasG	673.80	kJ/mol	NIST
μ	0.90	debye	KDB
ΔfG°	-33.08	kJ/mol	KDB
Rg	0.6040		KDB
ΔfH°gas	[-20.60; 20.18]	kJ/mol
ΔfH°gas	20.18	kJ/mol	KDB
ΔfH°gas	-20.60 ± 0.50	kJ/mol	NIST
ΔvapH°	7.72	kJ/mol	Relay (1.0) Calculated Property
IE	[10.00; 20.80]	eV
IE	10.46 ± 0.01	eV	NIST
IE	10.45 ± 0.01	eV	NIST
IE	10.46 ± 0.00	eV	NIST
IE	10.45 ± 0.01	eV	NIST
IE	10.00 ± 4.00	eV	NIST
IE	10.48	eV	NIST
IE	10.47 ± 0.00	eV	NIST
IE	10.56 ± 0.05	eV	NIST
IE	10.50	eV	NIST
IE	10.43	eV	NIST
IE	10.45	eV	NIST
IE	10.47	eV	NIST
IE	10.43	eV	NIST
IE	12.76	eV	NIST
IE	14.91	eV	NIST
IE	Outlier 20.80	eV	NIST
IE	18.00	eV	NIST
IE	12.81	eV	NIST
IE	14.79	eV	NIST
IE	10.43 ± 0.01	eV	NIST
IE	10.42	eV	NIST
IE	12.62	eV	NIST
IE	14.82	eV	NIST
IE	18.00	eV	NIST
IE	Outlier 20.12	eV	NIST
IE	10.45 ± 0.03	eV	NIST
IE	10.46 ± 0.01	eV	NIST
IE	10.47 ± 0.01	eV	NIST
IE	10.50	eV	NIST
IE	10.43	eV	NIST
IE	10.47	eV	NIST
IE	10.48	eV	NIST
log10WS	-2.02		Relay (1.0) Calculated Property
logPoct/wat	0.113		Crippen Calculated Property
McVol	27.210	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	3		KDB
Pc	[8940.00; 8970.00]	kPa
Pc	8940.00	kPa	KDB
Pc	8970.00 ± 18.00	kPa	NIST
Pc	8962.91 ± 30.00	kPa	NIST
Ptriple	[23.18; 23.20]	kPa
Ptriple	23.18	kPa	KDB
Ptriple	23.20 ± 0.50	kPa	NIST
ρc	347.63 ± 3.41	kg/m3	NIST
Inp	[338.00; 340.00]
Inp	340.00		NIST
Inp	338.00		NIST
Inp	338.00		NIST
I	[480.00; 480.00]
I	480.00		NIST
I	480.00		NIST
I	480.00		NIST
S°gas,1 bar	205.81 ± 0.05	J/mol×K	NIST
Tboil	[212.87; 213.60]	K
Tboil	213.60	K	KDB
Tboil	212.87 ± 0.07	K	NIST
Tc	[373.20; 373.40]	K
Tc	373.20	K	KDB
Tc	373.30 ± 0.37	K	NIST
Tc	373.40 ± 0.15	K	NIST
Tfus	[187.60; 190.85]	K
Tfus	187.60	K	KDB
Tfus	190.85 ± 1.50	K	NIST
Ttriple	[187.61; 187.67]	K
Ttriple	187.67	K	KDB
Ttriple	187.66 ± 0.06	K	NIST
Ttriple	187.61 ± 0.03	K	NIST
Vc	0.099	m3/kmol	KDB
Zc	0.2852290		KDB
Zra	0.28		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0000119; 0.0000268]	Pa×s	[291.61; 682.03]
η	0.0000119	Pa×s	291.61	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000119	Pa×s	292.30	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000119	Pa×s	292.46	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000119	Pa×s	292.77	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000121	Pa×s	296.89	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000121	Pa×s	297.01	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000132	Pa×s	323.94	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000132	Pa×s	323.96	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000143	Pa×s	350.47	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000143	Pa×s	350.59	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000154	Pa×s	378.01	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000154	Pa×s	378.19	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000166	Pa×s	405.76	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000166	Pa×s	405.86	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000177	Pa×s	433.66	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000177	Pa×s	433.81	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000188	Pa×s	461.72	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000188	Pa×s	461.92	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000199	Pa×s	490.09	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000199	Pa×s	490.20	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000210	Pa×s	518.68	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000210	Pa×s	518.75	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000219	Pa×s	542.48	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000219	Pa×s	542.61	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000227	Pa×s	565.19	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000228	Pa×s	565.29	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000238	Pa×s	593.95	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000238	Pa×s	594.02	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000248	Pa×s	623.07	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000248	Pa×s	623.19	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000258	Pa×s	652.30	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000258	Pa×s	652.32	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000268	Pa×s	681.36	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
η	0.0000268	Pa×s	682.03	Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
ΔsubH	[22.50; 25.40]	kJ/mol	[135.00; 175.50]
ΔsubH	22.50	kJ/mol	135.00	NIST
ΔsubH	25.40	kJ/mol	175.50	NIST
ΔvapH	[18.60; 21.90]	kJ/mol	[200.00; 295.50]
ΔvapH	21.90	kJ/mol	200.00	NIST
ΔvapH	19.50	kJ/mol	206.50	NIST
ΔvapH	18.60	kJ/mol	295.50	NIST
Pvap	[167.30; 8932.10]	kPa	[222.83; 373.15]
Pvap	167.30	kPa	222.83	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	167.40	kPa	223.19	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	209.10	kPa	228.20	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	257.40	kPa	233.11	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	313.90	kPa	238.04	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	384.00	kPa	243.02	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	380.10	kPa	243.04	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	380.20	kPa	243.18	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	379.40	kPa	243.20	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	456.70	kPa	248.01	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	544.20	kPa	252.97	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	644.50	kPa	258.01	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	757.70	kPa	263.00	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	885.70	kPa	268.02	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1033.00	kPa	273.08	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	1030.20	kPa	273.12	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	1029.30	kPa	273.13	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	1032.30	kPa	273.17	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1194.10	kPa	278.24	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1371.10	kPa	283.26	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1566.60	kPa	288.31	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1767.90	kPa	293.10	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1779.50	kPa	293.30	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	1793.70	kPa	293.43	Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
Pvap	2024.00	kPa	298.40	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	2022.20	kPa	298.41	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	2259.60	kPa	303.08	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	2847.20	kPa	313.11	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	3540.40	kPa	323.18	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	3564.00	kPa	323.50	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	4339.50	kPa	333.17	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	5261.20	kPa	343.16	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	5812.00	kPa	348.45	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	6319.20	kPa	353.17	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	7533.00	kPa	363.16	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Pvap	8932.10	kPa	373.15	Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
ρl	906.00	kg/m3	222.00	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[22.75; 8960.69]	kPa	[187.68; 373.53]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.43785e+01
Coefficient B			-1.84720e+03
Coefficient C			-2.35400e+01
Temperature range, min.			187.68
Temperature range, max.			373.53
Pvap	22.75	kPa	187.68	Calculated Property
Pvap	80.02	kPa	208.33	Calculated Property
Pvap	218.56	kPa	228.98	Calculated Property
Pvap	496.84	kPa	249.63	Calculated Property
Pvap	984.42	kPa	270.28	Calculated Property
Pvap	1754.98	kPa	290.93	Calculated Property
Pvap	2879.79	kPa	311.58	Calculated Property
Pvap	4422.55	kPa	332.23	Calculated Property
Pvap	6436.08	kPa	352.88	Calculated Property
Pvap	8960.69	kPa	373.53	Calculated Property

Similar Compounds

Find more compounds similar to Hydrogen sulfide.

Mixtures

• Hydrogen sulfide + Heptane
• Ethane, (methylthio)- + Hydrogen sulfide
• Carbon disulfide + Hydrogen sulfide
• Dimethyl sulfide + Hydrogen sulfide
• Ethane + Hydrogen sulfide
• Propane + Hydrogen sulfide
• Butane + Hydrogen sulfide
• Hydrogen sulfide + Thiophene, tetrahydro-, 1,1-dioxide
• Thiodiglycol + Hydrogen sulfide
• Hydrogen sulfide + Pentane
• sulfur + Hydrogen sulfide
• 1,2-Ethanediol + Hydrogen sulfide
• Triethylene glycol + Hydrogen sulfide
• Carbon dioxide + Hydrogen sulfide
• Hydrogen sulfide + Dimethyl Sulfoxide
• Formamide, N,N-dimethyl- + Hydrogen sulfide
• Methane + Hydrogen sulfide
• 2-Propanol, 1-amino- + Hydrogen sulfide + Water
• Hydrogen sulfide + Methyldiethanolamine + Water
• Hydrogen sulfide + Water + Thiophene, tetrahydro-, 1,1-dioxide

Find more mixtures with Hydrogen sulfide.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Solubility of Hydrogen Sulfide in [bmim][PF6]
• Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
• 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)
• The solubility of H2S in liquid sulfur
• Separation of CO2 and H2S using room-temperature ionic liquid [bmim][PF6]
• Solubility of H2S in 1-(2-hydroxyethyl)-3-methylimidazolium ionic liquids with different anions
• The diffusion coefficient of H2S in liquid sulfur
• Experimental study and phase equilibrium modeling of systems containing acid gas and glycol
• Measurements of H2S solubility in aqueous diisopropanolamine solutions and vapour pressure of diisopropanolamine
• Vapour-liquid equilibrium data for the hydrogen sulphide(H2S) + carbon dioxide (CO2) system at temperatures from 258 to 313 K
• Experimental solubility of hydrogen sulfide and carbon dioxide in dimethylformamide and dimethylsulfoxide
• Experimental study and thermodynamical modelling of thesolubilities of SO2, H2S and CO2in N-dodecylimidazole and 1,1 -[oxybis(2,1-ethanediyloxy-2,1-ethanediyl)]bis(imidazole): An evaluation of their potential application in the separation of acidic gases
• Phase equilibrium data for the hydrogen sulphide + methane system at temperatures from 186 to 313 K and pressures up to about 14 MPa
• Densities and derived thermophysical properties of the 0.9505 CO2 + 0.0495 H2S mixture from 273 K to 353 K and pressures up to 41 MPa
• Experimental and modelling study of the densities of the hydrogen sulphide + methane mixtures at 253, 273 and 293 K and pressures up to 30 MPa.
• Solubility of carbon dioxide and hydrogen sulfide in the ionic liquid 1-butyl-3-methylimidazolium trifluoromethanesulfonate
• Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K
• Solubility of H2S in ionic liquids [hmim][PF6], [hmim][BF4], and [hmim][Tf2N]
• Equilibrium solubility of H2S in aqueous solutions of 1-amino-2-propanol as function of concentration, temperature, and pressure
• Study of the solubility of CO2, H2S and their mixture in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate: Experimental and modelling
• Solubility of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl)trifluorophosphate
• Measuring the solubility of CO2 and H2S in sulfolane and the density and viscosity of saturated liquid binary mixtures of (sulfolane + CO2) and (sulfolane + H2S)
• High pressure measurement and CPA equation of state for solubility of carbon dioxide and hydrogen sulfide in 1-butyl-3-methylimidazolium acetate
• Measuring solubility of hydrogen sulphide in aqueous blends of N-methyldiethanolamine and 2-((2 aminoethyl)amino)ethanol and correlating by the Deshmukh-Mather model
• Measuring the density and viscosity of H2S-loaded aqueous methyldiethanolamine solution
• Experimental investigation of hydrogen sulfide solubility in aqueous sulfolane solution
• Measuring and correlating solubility of hydrogen sulfide in aqueous solution of 2-((2 aminoethyl)amino)ethanol
• Solubility of H2S and CO2 in imidazolium-based ionic liquids with bis(2-ethylhexyl) sulfosuccinate anion
• Measuring and modelling the absorption and volumetric properties of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium tetrafluoroborate
• Experimental diffusion coefficients of CO2 and H2S in some ionic liquids using semi-infinite volume method
• Experimental solubility of carbon dioxide and hydrogen sulfide in 2,2'-thiodiglycol
• Experimental and modelling investigation of H2S solubility in N-methylimidazole and gamma-butyrolactone
• Isothermal Vapor-Liquid Equilibrium (VLE) and Vapor- Liquid-Liquid Equilibrium (VLLE) Data for Two Binary Systems Containing Perfluorohexane with Carbon Monoxide or Hydrogen Sulphide at (293, 313 and 333) K
• The Solubility of Hydrogen Sulfide and Carbon Dioxide in Propylene Carbonate
• Solubility of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
• Evaluation of Methanesulfonate-Based Deep Eutectic Solvent for Ammonia Sorption
• P-rho-T and VLE for Ethane + Hydrogen Sulfide from (254.05 to 363.21) K at Pressures up to 20 MPa
• Separation of CO2 and H2S Using Room-Temperature Ionic Liquid [bmim][MeSO4]
• Solubility of H2S in Ionic Liquids 1-Ethyl-3-methylimidazolium Hexafluorophosphate ([emim][PF6]) and 1-Ethyl-3-methylimidazolium Bis(trifluoromethyl)sulfonylimide ([emim][Tf2N])
• P.rho.T Data for Hydrogen Sulfide + Propane from (263 to 363) K at Pressures up to 40 MPa
• Reference Viscosities of Gaseous Methane and Hydrogen Sulfide at Low Density in the Temperature Range from (292 to 682) K
• Solubility of H2S in Aqueous Diisopropanolamine + Piperazine Solutions: New Experimental Data and Modeling with the Electrolyte Cubic Square-Well Equation of State
• Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
• Solubility of Hydrogen Sulfide in N-Methylacetamide and N,N-Dimethylacetamide: Experimental Measurement and Modeling
• Isothermal Vapor Liquid Equilibrium Data and Thermodynamic Modeling for Binary Systems of Perfluorobutane (R610) + (Methane or Hydrogen Sulfide) at (293, 313, and 333) K
• Solubility of H2S in Ionic Liquids [bmim][PF6], [bmim][BF4], and [bmim][Tf2N]
• Article Solubility and Diffusion of H2S and CO2 in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate
• Solubility of Hydrogen Sulfide in Aqueous Solutions of Piperazine in the Low Gas-Loading Region
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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