Solubility of triethylene glycol in supercritical CO2

Solubility of Solids and Liquids in Supercritical Fluids

“…Other relevant references for the saturation method are the following: Czubryt (1970), Hemmaplardh and King (1972), Kwiatkowski et al (1984, Krukonis and Kurnik (1985), Moradinia and Teja (1986) and Pennisi and Chimowitz (1986). The subsequent list of recent references dealing with experimental investigations by the saturation method well documents the explosion of the activity in the field over the last few years: Cygnarowicz-Provost et al (1992), Hammam, H., (1992), Kramer and Thodos (1988), Iwai et al (1990), Jennings et al(1992, Li et al(1991), Hartland (1992), M'Hamdi et al (1992), Rijkers et al (1992aRijkers et al ( -1992b, Sakaki (1992), Schaeffer et al (1988), Smith and Wormald (1990), Suzuki et al (1991), Tan et al (1991), Wells et al (1990), Yau and Tsai (1992), Yokoyama et al (1992) and Yonemoto et al (1990), Gurdial and Foster (1991), Cross at al. (1996), Subra et al (1997), Sauceau et al (2000), Rodrigues et al (2000).…”

Modelling phase equilibria for acid gas mixtures using the CPA equation of state. Part VI. Multicomponent mixtures with glycols relevant to oil and gas and to liquid or supercritical CO 2 transport applications

“…Subsequently, in order to adjust the binary parameters, data for (CO 2 + MEG) were taken from Adachi et al [18], Oyevaar et al [19], Kaminishi et al [20], Jou et al [16] and Zheng et al [21]. The experimental data for (CO 2 + DEG) were obtained from Kaminishi et al [20], Jou et al [17] and Takahashi et al [22], while those for (CO 2 + TEG) were taken from Kaminishi et al [20], Yonemoto et al [23] and Davis et al [24].…”

Thermodynamic Modeling and Simulation of Natural Gas Dehydration Using Triethylene Glycol with the UMR-PRU Model

“…Experimental points by Jou et al: (Δ) at 298.15 K, (○) at 323.15 K, and (◇) at 373.15 K. (b) Methane/TEG mixture: (Δ) experimental points by Wilson et al at 298.15 K, (○) by Jou et al at 323.15 K, and (◇) by Jou et al at 373.15 K. (c) Vapor phase of the CO 2 /TEG mixture. Experimental points (○) at 313.15 K by Kaminishi et al and Yonemoto et al, (Δ) at 323.15 K by Yonemoto et al, and (◇) at 333.15 K by Kaminishi et al and Yonemoto et al (d) Vapor phase of the methane/TEG mixture. Experimental points by Jerinic et al.…”