TY - JOUR
T1 - Crystal Growth of Clathrate Hydrate Formed with Carbon Dioxide and Deuterium Oxide
T2 - Implications for Hydrate-based Tritium Separation
AU - Maruyama, Meku
AU - Dogi, Kaito
AU - Ohmura, Ryo
N1 - Publisher Copyright:
© 2024 American Chemical Society.
PY - 2024/4/4
Y1 - 2024/4/4
N2 - Tritium separation technology is a key method for treating contaminated water from nuclear power plants. Recently, a novel tritium separation method using deuterium oxide (D2O)-based clathrate hydrate has attracted attention because it can reduce the tritium concentration in contaminated water from 4.77 × 105 Bq/kg to 1.55 × 103 Bq/kg. In this hydrate-based tritium separation method, tritium is concentrated on the surface of a D2O-based hydrate substrate. The mechanistic characteristics and formation kinetics of D2O-based hydrates need to be clarified to develop an efficient process for substrate formation. This study contributes to the process design by revealing the crystal growth of the CO2 + D2O hydrate. The crystal growth behavior of the hydrate formed in the CO2 + D2O system was experimentally observed under different subcooling temperatures (ΔTsub) at 3.0 MPa. At all ΔTsub, hydrate crystals were formed at the gas-liquid interface and extended along the interface. After the interface was covered, hydrate crystals grew in the liquid phase. The variation in the morphology of CO2 + D2O hydrate depended on ΔTsub. At ΔTsub = 1.6 K, polygonal crystals with side lengths of 0.2-0.6 mm were formed. At ΔTsub = 2.7 K, columnar crystals with a length of 1-2 mm were formed. At ΔTsub ≥ 3.3 K, dendritic crystals were formed. With an increase in ΔTsub, the size of the dendritic branches increased. The crystal growth dynamics and morphological tendency of the CO2 + D2O hydrate were comparable to those of the CO2 + H2O hydrate at fixed ΔTsub. Detailed theoretical discussions on the obtained results of surface kinetics, mass transfer, and heat transfer during hydrate formation from H2O and D2O were provided, considering the chemical potential, viscosity, and heat transfer of the liquids.
AB - Tritium separation technology is a key method for treating contaminated water from nuclear power plants. Recently, a novel tritium separation method using deuterium oxide (D2O)-based clathrate hydrate has attracted attention because it can reduce the tritium concentration in contaminated water from 4.77 × 105 Bq/kg to 1.55 × 103 Bq/kg. In this hydrate-based tritium separation method, tritium is concentrated on the surface of a D2O-based hydrate substrate. The mechanistic characteristics and formation kinetics of D2O-based hydrates need to be clarified to develop an efficient process for substrate formation. This study contributes to the process design by revealing the crystal growth of the CO2 + D2O hydrate. The crystal growth behavior of the hydrate formed in the CO2 + D2O system was experimentally observed under different subcooling temperatures (ΔTsub) at 3.0 MPa. At all ΔTsub, hydrate crystals were formed at the gas-liquid interface and extended along the interface. After the interface was covered, hydrate crystals grew in the liquid phase. The variation in the morphology of CO2 + D2O hydrate depended on ΔTsub. At ΔTsub = 1.6 K, polygonal crystals with side lengths of 0.2-0.6 mm were formed. At ΔTsub = 2.7 K, columnar crystals with a length of 1-2 mm were formed. At ΔTsub ≥ 3.3 K, dendritic crystals were formed. With an increase in ΔTsub, the size of the dendritic branches increased. The crystal growth dynamics and morphological tendency of the CO2 + D2O hydrate were comparable to those of the CO2 + H2O hydrate at fixed ΔTsub. Detailed theoretical discussions on the obtained results of surface kinetics, mass transfer, and heat transfer during hydrate formation from H2O and D2O were provided, considering the chemical potential, viscosity, and heat transfer of the liquids.
UR - http://www.scopus.com/inward/record.url?scp=85188520527&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85188520527&partnerID=8YFLogxK
U2 - 10.1021/acs.energyfuels.4c00208
DO - 10.1021/acs.energyfuels.4c00208
M3 - Article
AN - SCOPUS:85188520527
SN - 0887-0624
VL - 38
SP - 6215
EP - 6222
JO - Energy and Fuels
JF - Energy and Fuels
IS - 7
ER -