TY - JOUR
T1 - Solubility of hydrogen sulfide in isooctane, n-decane, n-tridecane, n-hexadecane and squalane at temperatures from 323 to 523 K and pressures up to 1.6 MPa
AU - Yokoyama, Chiaki
AU - Usui, Akito
AU - Takahashi, Shinji
PY - 1993/5/15
Y1 - 1993/5/15
N2 - Yokoyama, C., Usui, A. and Takahashi, S., 1993. Solubility of hydrogen sulfide in isooctane, n-decane, n-tridecane, n-hexadecane and squalane at temperatures from 323 to 523 K and pressures up to 1.6 MPa. Fluid Phase Equilibria, 85: 257-269. The solubility of hydrogen sulfide (H2S) in isooctane, n-decane, n-tridecane, n-hexadecane and squalane has been experimentally determined for the temperature range 323-523 K and pressures up to 1.6 MPa. Henry's constants have been determined from the solubility data according to the Krichevsky-Kasanovsky equation. The Soave-Redlich-Kwong (SRK) and the Peng-Robinson (PR) equations of state were used to calculate the solubility data. The binary interaction parameter of the PR equation was correlated with the ratio of the critical volumes of H2S and hydrocarbons.
AB - Yokoyama, C., Usui, A. and Takahashi, S., 1993. Solubility of hydrogen sulfide in isooctane, n-decane, n-tridecane, n-hexadecane and squalane at temperatures from 323 to 523 K and pressures up to 1.6 MPa. Fluid Phase Equilibria, 85: 257-269. The solubility of hydrogen sulfide (H2S) in isooctane, n-decane, n-tridecane, n-hexadecane and squalane has been experimentally determined for the temperature range 323-523 K and pressures up to 1.6 MPa. Henry's constants have been determined from the solubility data according to the Krichevsky-Kasanovsky equation. The Soave-Redlich-Kwong (SRK) and the Peng-Robinson (PR) equations of state were used to calculate the solubility data. The binary interaction parameter of the PR equation was correlated with the ratio of the critical volumes of H2S and hydrocarbons.
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U2 - 10.1016/0378-3812(93)80018-I
DO - 10.1016/0378-3812(93)80018-I
M3 - Article
AN - SCOPUS:0027596026
VL - 85
SP - 257
EP - 269
JO - Fluid Phase Equilibria
JF - Fluid Phase Equilibria
SN - 0378-3812
IS - C
ER -