2008
DOI: 10.1016/j.jct.2008.04.009
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Gas hydrate equilibrium dissociation conditions in porous media using two thermodynamic approaches

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Cited by 110 publications
(91 citation statements)
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References 25 publications
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“…As shown in Figure 3, the stable pressure for experiments 4, 5a, 6 and 7 are 12.44, 12.50, 12.52 and 12.75 MPa respectively. As calculated by Li et al [24], the equilibrium formation pressure for bulk methane hydrate at the temperature of 276.15 K is only 3.50 MPa. It can be seen that, the pressure inside the crystallizer gradually decreases and reaches stable at a higher pressure than the equilibrium hydrate formation pressure for bulk hydrate, resulting in a relatively lower water conversion to hydrate.…”
Section: Methodsmentioning
confidence: 82%
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“…As shown in Figure 3, the stable pressure for experiments 4, 5a, 6 and 7 are 12.44, 12.50, 12.52 and 12.75 MPa respectively. As calculated by Li et al [24], the equilibrium formation pressure for bulk methane hydrate at the temperature of 276.15 K is only 3.50 MPa. It can be seen that, the pressure inside the crystallizer gradually decreases and reaches stable at a higher pressure than the equilibrium hydrate formation pressure for bulk hydrate, resulting in a relatively lower water conversion to hydrate.…”
Section: Methodsmentioning
confidence: 82%
“…No multistage was observed in the hydrate formation process at the water saturation of 40%. Because the equilibrium hydrate formation pressure increases and the driving force of the hydrate formation decreases as the temperature increases, it should be caused by the difference of the driving force for the hydrate formation [24]. As shown in Table 4, the final water conversion in the experiments at the water saturation of 40% only ranges from 35.98% to 48.98%.…”
Section: Methodsmentioning
confidence: 96%
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“…When PW decreases from 4.5 to 3.4 MPa, the volume of gas production increases by 20.5%, and when PW decreases from 3.4 to 2.3 MPa, the volume of gas production increases by 13.6%. Additionally, the lowest PW is 2.3 MPa, which is lower than the quadruple point of methane hydrate (2.60 MPa [51]). However, the ice blocking does not happen in this case.…”
Section: Sensitivity Analysis Of Production From Gmgs2-site 8 In Pearmentioning
confidence: 78%
“…Before hydrate production, the initial hydrate/water/gas saturations (volume) are calculated as 38.5%, 2.2%, and 59.3%, respectively, using the model proposed by Linga et al [13]. During the hydrate production, the temperature of the water bath is maintained at 8.0 °C, and the corresponding equilibrium pressure is calculated to be 5.7 MPa by the fugacity model proposed by Li et al [14]. The temperature of deionized water is raised to the injection temperature (T i = 130 °C) in the pre-heater.…”
Section: Experimental Methodsmentioning
confidence: 99%