The three-phase, hydrate-water-rich liquid-vapor (HLV), equilibria of the b
inary guest mixtures containing CO2 and N-2 were determined at the temperat
ure range of 272-275 K and different compositions of vapor phase. In additi
on, two phase equilibria of hydrate and vapor were also measured at three i
sothermal conditions of 274, 277 and 278 K. The resulting P-x diagram indic
ates that CO2 can be more contained than N-2 in the hydrate phase. More tha
n 96 mol% CO2 in the mixed hydrate phase was obtained from a gas mixture of
17 mol% CO2 and 83 mol% of N-2 at 274 K. The addition of tetrahydrofuran (
THF) as a hydrate promoter extended hydrate stability region by elevating e
quilibrium dissociation temperature and lowering pressure. The overall hydr
ate equilibrium results were found to agree well with the calculated ones.
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