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带收缩-扩张导流叶片的两级内循环气升式反应器内流体动力学的计算流体动力学模拟

Computational Fluid Dynamics Simulation of Hydrodynamics in a Two-Stage Internal Loop Airlift Reactor with Contraction-Expansion Guide Vane.

作者信息

Shi Jiazhen, Guo Kai, Wang Zhengchao, Zheng Longyun, Liu Hui, Xiang Wenyu, Liu Chunjiang, Li Xue

机构信息

School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China.

State Key Laboratory of Chemical Engineering, Tianjin University, Tianjin 300072, China.

出版信息

ACS Omega. 2021 Mar 2;6(10):6981-6995. doi: 10.1021/acsomega.0c06277. eCollection 2021 Mar 16.

Abstract

Global circulation and liquid back mixing adversely affect the continuous production of a multistage internal airlift loop reactor. A contraction-expansion guide vane (CEGV) is proposed and combined with a two-stage internal loop airlift reactor (TSILALR) to suppress the liquid back mixing between stages. A computational fluid dynamics (CFD) simulation is conducted to evaluate the performance of the CEGV in the TSILALR. The bubble size distribution and turbulent flow properties in the TSILALR are considered in the CFD simulation by using the population balance model and RNG - turbulence model. The CFD model is validated against the experimental results. The deviations in the gas holdup and mean bubble diameter between the simulation and experimental results are less than 8% and 6%, respectively. The streamlines, flow pattern, bubble size distribution, and axial liquid velocity in the TSILALRs with and without the CEGV at superficial velocities of 0.04 and 0.08 m/s are obtained by CFD simulation. It has been shown that the CEGV generated local circulation flows at each stage instead of a global circulation flow in the TSILALR. The average global gas holdup in the TSILALR with a CEGV increased up to 1.98 times. The global gas holdup increased from 0.045 to 0.101 and the average axial velocity in the riser decreased from 0.314 to 0.241 m/s when the width of the CEGV increased from 50 to 75 mm at the superficial gas velocity of 0.08 m/s.

摘要

整体循环和液体返混对多级内循环气升式环流反应器的连续生产产生不利影响。提出了一种收缩-扩张导流叶片(CEGV),并将其与两级内循环气升式反应器(TSILALR)相结合,以抑制级间液体返混。进行了计算流体动力学(CFD)模拟,以评估CEGV在TSILALR中的性能。在CFD模拟中,通过使用群体平衡模型和RNG湍流模型来考虑TSILALR中的气泡尺寸分布和湍流特性。CFD模型根据实验结果进行了验证。模拟结果与实验结果在气含率和平均气泡直径方面的偏差分别小于8%和6%。通过CFD模拟获得了在表观气速为0.04和0.08 m/s时,有无CEGV的TSILALR中的流线、流型、气泡尺寸分布和轴向液体速度。结果表明,CEGV在TSILALR的每个阶段产生局部循环流,而不是整体循环流。带有CEGV的TSILALR中的平均整体气含率提高到了1.98倍。在表观气速为0.08 m/s时,当CEGV的宽度从50 mm增加到75 mm时,TSILALR中的整体气含率从0.045增加到0.101,提升管中的平均轴向速度从0.314 m/s降低到0.241 m/s。

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