TY - JOUR
T1 - Synthesis of CO2 hydrate capsules in partially water-saturated sediment as vessels for underground mechanical energy storage
T2 - Promoting effect of tetrahydrofuran and cyclopentane
AU - Ouyang, Qian
AU - Lev-Yehudi, Omer
AU - Pandey, Jyoti Shanker
AU - Franza, Andrea
AU - Rocchi, Irene
AU - Klar, Assaf
AU - von Solms, Nicolas
N1 - Publisher Copyright: © 2025
PY - 2025/8
Y1 - 2025/8
N2 - The intermittency of renewable energy sources and the increase in renewable energy shares require energy storage capability to sustain the green transition. One promising solution for underground energy storage is the use of subsurface CO2 hydrate capsules, which act as impermeable vessels that store compressed fluids and discharge them upon need. However, as part of the proof-of-concept study of this technology, the feasibility of constructing such vessels, e.g. CO2 hydrate capsules, has yet to be demonstrated. This work employed CO2 gas injection assisted by chemical solution into partially water-saturated sand sediments to synthesize CO2 hydrate capsules. The concentrations of chemical solutions (THF, CP and DIOX) were screened out in the gas/liquid/sand system in terms of kinetic promotion, using a rocking cell. Separately, experiments were carried out with a new high-pressure chamber set-up that quantified the effects of water saturation and chemical promoters on the efficiencies of CO2 hydrate synthesis in confined partially water-saturated sand. Results on the gas/liquid/sand system showed that 0.025 water/CP weight ratio CP solution and 1.3mol% THF solution induced the largest pressure drops of 18.4 ± 0.2 bar and 16.7 ± 0.1 bar, respectively, indicating the most promoted CO2 hydrate formation kinetics. Results with the pressure chamber showed three stages during slow CO2 gas injection: (1) initial pressure “build-up stage”; subsequent (2) CO2 gas “uptake stage”; and (3) CO2 injection “closing stage”. CO2 hydrate formation kinetics of CO2 hydrate retention percentage (SCO2) and CO2 hydrate density (ρCO2) were directly proportional to the initial water saturation (6.0–76.7%). Injection of THF or CP solutions increased SCO2 by 16.5% or 18.5%, and ρCO2 by 74.5% or 128.3% compared to injection of water. The best performances were obtained at a fluid pressure of 27.0 bar, with a 0.025 water/CP solution-assisting CO2 gas injection, in sediment with an initial water saturation of 32.6% and porosity of 44.6%, giving rise to SCO2 of 67.2% and ρCO2 of 80.6%. These findings demonstrated that the injection of THF or CP solution with CO2 gas facilitated the possibility of the formation and stabilization of subsurface CO2 hydrate capsules.
AB - The intermittency of renewable energy sources and the increase in renewable energy shares require energy storage capability to sustain the green transition. One promising solution for underground energy storage is the use of subsurface CO2 hydrate capsules, which act as impermeable vessels that store compressed fluids and discharge them upon need. However, as part of the proof-of-concept study of this technology, the feasibility of constructing such vessels, e.g. CO2 hydrate capsules, has yet to be demonstrated. This work employed CO2 gas injection assisted by chemical solution into partially water-saturated sand sediments to synthesize CO2 hydrate capsules. The concentrations of chemical solutions (THF, CP and DIOX) were screened out in the gas/liquid/sand system in terms of kinetic promotion, using a rocking cell. Separately, experiments were carried out with a new high-pressure chamber set-up that quantified the effects of water saturation and chemical promoters on the efficiencies of CO2 hydrate synthesis in confined partially water-saturated sand. Results on the gas/liquid/sand system showed that 0.025 water/CP weight ratio CP solution and 1.3mol% THF solution induced the largest pressure drops of 18.4 ± 0.2 bar and 16.7 ± 0.1 bar, respectively, indicating the most promoted CO2 hydrate formation kinetics. Results with the pressure chamber showed three stages during slow CO2 gas injection: (1) initial pressure “build-up stage”; subsequent (2) CO2 gas “uptake stage”; and (3) CO2 injection “closing stage”. CO2 hydrate formation kinetics of CO2 hydrate retention percentage (SCO2) and CO2 hydrate density (ρCO2) were directly proportional to the initial water saturation (6.0–76.7%). Injection of THF or CP solutions increased SCO2 by 16.5% or 18.5%, and ρCO2 by 74.5% or 128.3% compared to injection of water. The best performances were obtained at a fluid pressure of 27.0 bar, with a 0.025 water/CP solution-assisting CO2 gas injection, in sediment with an initial water saturation of 32.6% and porosity of 44.6%, giving rise to SCO2 of 67.2% and ρCO2 of 80.6%. These findings demonstrated that the injection of THF or CP solution with CO2 gas facilitated the possibility of the formation and stabilization of subsurface CO2 hydrate capsules.
KW - CO retention
KW - Gas hydrate
KW - Hydrate promoter
KW - Injection
KW - Kinetics
UR - http://www.scopus.com/inward/record.url?scp=105000479312&partnerID=8YFLogxK
U2 - 10.1016/j.fluid.2025.114428
DO - 10.1016/j.fluid.2025.114428
M3 - مقالة
SN - 0378-3812
VL - 595
JO - Fluid Phase Equilibria
JF - Fluid Phase Equilibria
M1 - 114428
ER -