Heat transfer at low temperatures

Abstract

The non-condensable gas at the top of the main condenser of the distillation section, such as helium or neon, would lower the heat transfer efficiency and the productivity of the air separation plant. Current research mainly focuses on the study of the water vapor condensation mechanism with non-condensable gases, while those on cryogenic fluids are rare. In this work, an experimental setup was designed to study the condensation mechanism of pure nitrogen vapor and nitrogen vapor mixed with helium on the vertical plate. The experimental data of pure nitrogen vapor is in good agreement with the results calculated by the classical Nusselt model, which demonstrates that the experimental system has high reliability. The influences of the mass fraction of helium and system pressure on the condensation heat transfer coefficient are analyzed. Results show that even a very low mass fraction of helium can cause the condensation heat transfer coefficient of nitrogen vapor to decrease obviously. The deviation between the heat transfer coefficient of the nitrogen-helium mixture and pure nitrogen increases with the increases of the helium mass fraction and the decrease of system pressure. A new condensation heat transfer correlation for nitrogen with helium is developed that the deviations of most of its predictions are within 20% compared to the experimental data.