列管式固定床反应器管束间单相流动与传热的CFD研究  

CFD Simulation of Fluid Flow and Heat Transfer of Single Phase inside the Shell Side of Multitubular Fixed Bed Reactor

作　　者：张敏华[1] 百璐[1] 耿中峰[1] 李永辉[1] 

机构地区：[1]天津大学石油化工技术开发中心绿色合成与转化教育部重点实验室,天津300072

出　　处：《高校化学工程学报》2013年第2期222-227,共6页Journal of Chemical Engineering of Chinese Universities

摘　　要：为研究列管式固定床反应器壳程内换热介质的流动与传热特性,采用数值模拟的方法求解得到壳程流体速度与温度分布场。模拟结果受湍流模型影响,将壳程传热膜系数和压降的CFD模拟结果与经验方法结果进行比较后选择偏差最小的realizable k-ε湍流模型。模拟结果显示换热介质在反应器壳程内的流动与传热分布不均匀,折流板前背部存在漩涡和传热死区,错流区和折流板缺口区的传热效果较好。为验证CFD模拟结果的可靠性,将不同传热量和进口流量条件下的模拟结果与经验方法结果进行比较,偏差在可接受范围内。The numerical simulation method （commercial CFD code） was used to investigate the fluid flow and heat transfer inside the shell side of multitubular fixed bed reactor. It was found that the simulation results are sensitive to the turbulence model selection, and realizable k-ε model was considered as the best turbulence model by comparing the CFD results of heat transfer coefficient and pressure drop with empirical method results. The simulation results show that the velocity and temperature distribution vary along axial and radial direction, and there are stagnation regions before and behind the baffles, in which the heat transfer coefficient is low; but high heat transfer was observed in cross flow zones and baffle cut zones. Finally, the validity of the CFD results was confirmed by comparing its results of outlet temperature, total pressure drop and average heat transfer coefficient with empirical method results under different heat flux and inlet velocity conditions. The calculating results have a good agreement with the results of empirical methods.

关 键 词：列管式固定床反应器 单相传热 CFD模拟 湍流模型 折流板 传热膜系数 

分 类 号：TQ051.14[化学工程] TQ021.3