2013
DOI: 10.1021/je400773k
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Phase Equilibria and Dissociation Enthalpies of Tri-n-butylphosphine Oxide Semiclathrate Hydrates Incorporated with CH4, CO2, and H2

Abstract: We investigated the phase equilibrium boundary of tri-n-butylphosphine oxide (TBPO) semiclathrate hydrates incorporated with CH 4 , CO 2 , and H 2 . TBPO aqueous solutions with a molality (m) of (1.61 and 1.98) mol·kg −1 were used for hydrate formation, which corresponded to the clathrate structures of TBPO· 34.5H 2 O and 28H 2 O, respectively. The phase boundary at both concentrations was shifted to the promotion region represented by lower pressures and higher temperatures, compared to each simple gas hydrat… Show more

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Cited by 12 publications
(7 citation statements)
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“…The temperature range of TBPO + CH 4 double hydrate preparation is limited by the dissociation temperature of TBPO + CH 4 hydrate, ∼296 K, and the melting point of the eutectic mixture in the TBPO–H 2 O system, ∼272.9 K . The synthesis of the double TBPO + CH 4 hydrates was carried out at a methane pressure of 8.5 ± 0.5 MPa and temperature of 274 ± 1 K that is somewhat higher than the eutectic melting point.…”
Section: Results and Discussionmentioning
confidence: 99%
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“…The temperature range of TBPO + CH 4 double hydrate preparation is limited by the dissociation temperature of TBPO + CH 4 hydrate, ∼296 K, and the melting point of the eutectic mixture in the TBPO–H 2 O system, ∼272.9 K . The synthesis of the double TBPO + CH 4 hydrates was carried out at a methane pressure of 8.5 ± 0.5 MPa and temperature of 274 ± 1 K that is somewhat higher than the eutectic melting point.…”
Section: Results and Discussionmentioning
confidence: 99%
“…It has been suggested that several hydrates can be formed in the system, and TBPO·28H 2 O was previously reported as their averaged composition. Most recently reported data on P , T hydrate phase equilibria for aqueous solutions of TBPO + CH 4 , , + CO 2 , , + N 2 , + H 2 , + simulated biogas (60 mol % CH 4 + 40 mol % CO 2 ), + simulated mine ventilation air (0.5 vol % CH 4 + 99.5 vol % air), + simulated flue gas (12.5 vol % CO 2 + 80.5 vol % N 2 + 6.9 vol % O 2 ) showed a shift of the hydrate phase equilibria to lower pressures and higher temperatures, compared to the corresponding gas + water system. These observations are evidence of the inclusion of gas molecules into the cavities of the TBPO hydrate structure.…”
Section: Introductionmentioning
confidence: 98%
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“…In the present work, the phase equilibrium conditions of ventilation air methane hydrate and ventilation air methane + TBAB or TBPO semi-clathrate hydrate at 5 wt%, 15 wt% and 26 wt% are tabulated in Table 1 [30,33]. Note also that with increasing the initial loading from 5 wt% to 26 wt%, the gap between the TBAB and TBPO curves became smaller as the pressure requirement for the formation of ventilation air methane hydrate was not sensitive to the initial TBPO loading but to the initial TBAB loading.…”
Section: Thermodynamic Stability Conditionsmentioning
confidence: 99%
“…Due to the vast quantity of methane contained in these hydrates, they have been considered a new source of hydrocarbon energy for future. Gas hydrates have also received much attention as new media for energy gas storage, transportation, and greenhouse gas separation and as phase changing materials for refrigeration and air conditioning. Additionally, the hydrate formation has been proposed as an alternative technique in desalinating seawater or frac water to produce fresh water. At the same time, the undesired formation of gas hydrates is known to be a serious problem in the gas and oil industry . In subsea production, gas hydrates form deposits in pipelines and cause plugging of the pipelines or other processing equipment.…”
Section: Introductionmentioning
confidence: 99%