2021
DOI: 10.1021/acs.jced.1c00063
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Effect of HFE254 or Cyclopentanone on Phase Equilibrium Dissociation Conditions for Carbon Dioxide Hydrate

Abstract: Hydrate equilibrium conditions of the CO2 + HFE254 or cyclopentanone + water system are determined by the isometric method. The presence of cyclopentanone promotes CO2 hydrate formation, while HFE254 does not affect the equilibrium pressure of CO2 hydrate. The hydrate dissociation temperature of the CO2 + cyclopentanone system increases as the pressure increases. However, the hydrate equilibrium temperature gradually decreases when pressure is above 3.2 MPa and a mixed hydrate of structure I and structure II f… Show more

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Cited by 6 publications
(3 citation statements)
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References 39 publications
(57 reference statements)
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“…By using the additive that is slightly soluble in water, the CO 2 + H 2 O + additive experimental system should have three constituents and four phases. According to the Gibbs phase rule, and the studies of Mooijer-Van Den Heuvel et al and Sun et al, , a four-phase equilibrium has one degree of freedom in ternary systems, and the concentration of the additive in the experimental system will not affect the equilibrium conditions of the hydrate system.…”
Section: Methodsmentioning
confidence: 99%
“…By using the additive that is slightly soluble in water, the CO 2 + H 2 O + additive experimental system should have three constituents and four phases. According to the Gibbs phase rule, and the studies of Mooijer-Van Den Heuvel et al and Sun et al, , a four-phase equilibrium has one degree of freedom in ternary systems, and the concentration of the additive in the experimental system will not affect the equilibrium conditions of the hydrate system.…”
Section: Methodsmentioning
confidence: 99%
“… a T exp. : Experimental equilibrium temperature of hydrate at corresponding pressure in the presence of promoter (CPN, NPA, FCP, HCFC141b, CH, HFC-134a, and CP , ). (*): Estimated from thermodynamic modeling. …”
Section: Simulation Methodologymentioning
confidence: 99%
“…It should be mentioned that CO 2 and NF 3 sI hydrates were simulated at 3/ 10 MPa and 273/283/293 K. In addition, simulations for the case of 75% cage occupancy filled by CO 2 and NF 3 molecules were performed at 3/10 MPa and 283 K. Also, the summary of simulation conditions and guest compositions in the initial configuration of CO 2 /CO 2 + CH 4 sII hydrates in the presence of different promoters is presented in Table 2. To provide the initial simulations, all small cages were filled with CO 2 or CH 4 58 NPA, 59 FCP, 60 HCFC141b, 61 CH, 62 HFC-134a, 63 and CP 41,42 ). (*): Estimated from thermodynamic modeling.…”
Section: Simulation Methodologymentioning
confidence: 99%