Evaluation of 1,3-dioxolane in promoting CO2 hydrate kinetics and its significance in hydrate-based CO2 sequestration

• Published in: Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2023-01, Vol.451, p.138799, Article 138799
• Main Authors: Yao, Yuanxin, Yin, Zhenyuan, Niu, Mengya, Liu, Xuejian, Zhang, Jibao, Chen, Daoyi
• Format: Article
• Language: English
• Subjects: 1,3-dioxolane; CO2 hydrate; Hydrate morphology; Kinetics; Phase equilibria; Raman spectroscopy
• ISSN: 1385-8947; 1873-3212
• DOI: 10.1016/j.cej.2022.138799

[Display omitted] •Phase equilibria of CO2 + DIOX hydrate for CDIOX between 0.05 mol% and 5.56 mol%•The kinetics of CO2 + DIOX hydrate is quantified with morphology observation.•Phase separation of DIOX/H2O above 3.1 MPa weakens the promotion effect of DIOX.•A comprehensive evaluation of DIOX in the application of hydrate-based CO2 storage. To reduce anthropogenic CO2 emissions for the mitigation of climate change require novel CCUS solutions. Hydrate-based CO2 sequestration (HCS) is a novel carbon-neutrality technology that aims to store CO2 in solid hydrate form with long-term stability. However, imminent issues exist for the application of HCS in terms of demanding thermodynamic conditions, slow formation kinetics, and low CO2 gas uptake. These challenges necessitate the quest for an efficient and eco-friendly CO2 hydrate promoter. In this study, 1,3-dioxolane (DIOX) as a low-toxicity CO2 hydrate promoter was systematically examined. The phase equilibria, cage occupancy, and the kinetics of binary CO2 + DIOX hydrate were measured for DIOX concentrations (CDIOX) varying from 0.05 mol% to 5.56 mol%. It was confirmed that DIOX is a dual-function promoter for CO2 hydrate, but its promotion effect is weakened for CDIOX between 0.60 mol% and 1.00 mol% and for all CDIOX at relatively high pressure. The CO2 uptake in the hydrate phase increases with CDIOX above 2.00 mol% and is the highest for CDIOX = 5.56 mol% (57.08 ± 6.39 mmol/mol). Based on the morphology observation, hydrate transits from ice-like to slurry to mushy-like and finally to snow-like with increasing CDIOX. Interestingly, we observed that the aqueous phase separates into two phases (i.e., DIOX-rich and H2O-rich) at pressure above 3.09 MPa, which explains the gradual loss of the promotion effect. The results of our study provide a comprehensive evaluation on DIOX as a possible promoter for CO2 hydrate in HCS application.