Insights into structure-performance relationship in radial flow fixed bed reactor for CO2 methanation

传热 甲烷化 机械 向心力 放热反应 流量(数学) 工作(物理) 努塞尔数 材料科学 化学 热力学 甲烷 物理 雷诺数 湍流 有机化学
作者
Wei Zhang,Yixiong Lin,Koyo Norinaga
出处
期刊:International Journal of Hydrogen Energy [Elsevier]
卷期号:48 (64): 24594-24606 被引量:2
标识
DOI:10.1016/j.ijhydene.2023.03.343
摘要

The extraction of petroleum and natural gas is often accompanied by a large number of associated gases, especially the high CO2 content reservoirs facing the emission of a large amount of CO2. CO2 methanation is recognized as one of the suitable candidates for CO2 utilization to reduce the emission of CO2. Because of the highly exothermic nature of the reaction, however, it is very important to enhance the heat transfer process inside the reactor and inhibit the formation of hot spots. In the fixed bed reactor, the heat transfer in the radial direction is greatly limited compared with that in the axial direction. Thus, this work adopted the radial flow reactor to evaluate the CO2 methanation process by the means of a numerical model based on OpenFOAM. Four types of radial flow reactor configurations, namely centrifugal Z-type, centrifugal Π-type, centripetal Z-type, and centripetal Π-type, were compared. The fluid flow, heat transfer, and reaction performances for these reactors were discussed under consistent operating conditions. Results show that the centrifugal Π-type structure has the most uniform flow field. In terms of heat transfer and reaction performance, the centripetal Z-type structure is the best among the four radial flow reactor configurations. These findings provide a theoretical basis and technical guidance for designing and developing radial flow reactors.
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