Abstract
The presence of non-condensable gas significantly deteriorates the heat transfer of water vapor condensation, and the condensation process of a CO2-water vapor mixture is a key process for CO2 separation and purification. In this study, we fabricated an experimental system to investigate the heat transfer characteristics of the mixed vapor condensation using a CO2 mass fraction of 32–85 % at a flow rate of 0.4–1.2 m/s and surface subcooling of 3–70 K. Liquid film thickness, gas-phase diffusion layer thickness, and interface temperature were calculated based on the double boundary layer model. An increase in the flow rate (0.4–1.2 m/s) improved the mixed vapor heat transfer, especially at high CO2 concentrations, and increased the heat transfer coefficient by 177 % at a surface subcooling of 40 K. The lower the surface subcooling, the greater the effect of the flow rate. As the CO2 concentration increased, the liquid film thickness decreased, whereas the gas-phase diffusion layer thickness increased to 1.7 mm, which is tens and hundreds of times the liquid film thickness. Increasing the flow rate slightly changed the liquid film but significantly reduced the gas-phase diffusion layer thickness and afforded a better heat transfer performance. A new heat transfer correlation equation was fitted, and the error of the predicted value was within ± 30 %. This study provides fundamental insights for the design of related heat exchangers.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.