Tritium separation technology is a key method for treating contaminated water from nuclear power plants. Recently, a novel tritium separation method using deuterium oxide (D 2 O)based clathrate hydrate has attracted attention because it can reduce the tritium concentration in contaminated water from 4.77 × 10 5 Bq/kg to 1.55 × 10 3 Bq/kg. In this hydrate-based tritium separation method, tritium is concentrated on the surface of a D 2 O-based hydrate substrate. The mechanistic characteristics and formation kinetics of D 2 O-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 CO 2 + D 2 O hydrate. The crystal growth behavior of the hydrate formed in the CO 2 + D 2 O system was experimentally observed under different subcooling temperatures (ΔT sub ) at 3.0 MPa. At all ΔT sub , 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 CO 2 + D 2 O hydrate depended on ΔT sub . At ΔT sub = 1.6 K, polygonal crystals with side lengths of 0.2−0.6 mm were formed. At ΔT sub = 2.7 K, columnar crystals with a length of 1−2 mm were formed. At ΔT sub ≥ 3.3 K, dendritic crystals were formed. With an increase in ΔT sub , the size of the dendritic branches increased. The crystal growth dynamics and morphological tendency of the CO 2 + D 2 O hydrate were comparable to those of the CO 2 + H 2 O hydrate at fixed ΔT sub . Detailed theoretical discussions on the obtained results of surface kinetics, mass transfer, and heat transfer during hydrate formation from H 2 O and D 2 O were provided, considering the chemical potential, viscosity, and heat transfer of the liquids.