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Experimental study demonstrates enhanced solubility of methane and carbon dioxide in a ternary aqueous system, suggesting non-ideal synergistic interactions under high pressure.
Reported are the experimental measurements on vapor–liquid equilibria in the H 2 O + CO 2 + CH 4 ternary system at temperatures from (324 to 375) K and pressures from (10 to 50) MPa. The results indicate that the CH 4 solubility in the ternary mixture is about 10 % to 40 % more than that calculated by interpolation from the Henry’s law constants of the binary system, H 2 O + CH 4, and the solubility of CO 2 is 6 % to 20 % more than what is calculated by the interpolation from the Henry’s law constants of the binary mixture, H 2 O + CO 2 .
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Qin et al. (2008) studied this question.
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