Identification of flow regime in a co-current upflow packed bed reactor (U-PBR) using gamma-ray densitometry (GRD)

被引:0
作者
Yatimi, Youssef [1 ]
Alalou, Ahmed [1 ,2 ]
Al-Dahhan, Muthanna [1 ,3 ,4 ]
机构
[1] Missouri Univ Sci & Technol, Linda & Bipin Doshi Dept Chem & Biochem Engn, Multiphase Flow & Reactors Engn & Educ Lab mFReel, Rolla, MO 65409 USA
[2] Univ Sidi Mohammed Ben Abdellah, Fac Sci & Tech, Lab Appl Organ Chem, BP 2202, Fes, Morocco
[3] Missouri Univ Sci & Technol, Dept Nucl Engn & Radiat Sci, Rolla, MO 65409 USA
[4] Mohammed VI Polytech Univ UM6P, Appl Chem & Engn Res Ctr Excellence ACER CoE, Lot 660, Ben Guerir 43150, Morocco
关键词
Upflow packed bed reactor; Flow regime; Gamma ray densitometry (GRD); Kolmogorov entropy; Standard deviation; GAS-LIQUID UPFLOW; TIME-SERIES ANALYSIS; BUBBLE-COLUMN; PRESSURE-DROP; MASS-TRANSFER; HEAT-TRANSFER; 2-PHASE FLOW; CO-CURRENT; DOWNFLOW; HYDRODYNAMICS;
D O I
10.1016/j.ces.2025.121871
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Owing to their significant impact on the reaction rate, the comprehensive understanding of the hydrodynamics in any novel design of the Upflow Packed Bed Reactor (U-PBR) is essential for the optimization of its throughput. In this regard, the identification of the flow regime is of paramount importance. Therefore, in this work, we use the photon counts time-series data obtained using the non-invasive Gamma-ray densitometry (GRD) to identify, for the first time, the flow regimes and their transition velocities at two axial locations (Z/D = 0.8, 1.56) and five radial locations (r/R = 0, +0.5, +0.9) within the packed catalysts' bed of U-PBR with a novel plenum design consisting of five deflectors. The photon counts, which were obtained for a wide range of superficial inlet gas velocities (0.06-9.6cm/s) and superficial inlet liquid velocities (0.003-0.021cm/s), were analyzed using the Kolmogorov Entropy (KE) method and the Standard Deviation method. Using these two methods, three flow regimes (bubble, pulse, and spray) as well as transient phases were identified at the center of the reactor (r/R = 0) at varying superficial inlet gas and liquid velocities depending on the axial location. At most other radial location, owing to more significant pressure drop, only two flow regimes are identified. Furthermore, the transition velocities were more distinctly identified using the KE method, compared to the standard deviation. These transition velocities were also found to vary significantly depending on the void fraction which substantially affects the liquid and gas distribution and mixing, as well as the local gas and liquid velocities.
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页数:17
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