实验室规模循环流化床提升管固相速度流场和固相混合与Geldart的B族颗粒和放大

IF 13.2 1区 工程技术 Q1 ENGINEERING, CHEMICAL
Trilokpati Tribedi, Premsagar Pillajetti, Pankaj Tiwari, Jayashree Biswal, V.K. Sharma, Rajesh Kumar Upadhyay
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引用次数: 0

摘要

采用放射性粒子跟踪这一无创速度测量技术,利用Geldart B族粒子对实验室规模循环流化床底部和中段冷流气固提升管内的固体速度流场进行了测量。在不同的进气速度和固体通量下,在不同的立管高度上,给出了固体平均速度、均方根速度和颗粒温度的径向分布。RPT数据表明,固体运动主要是沿轴向,平均径向运动几乎可以忽略不计。与径向均方根速度相比,轴向均方根速度明显更高。瞬时速度波动数据表明,当气速为6和6.5 m/s时,内部再循环明显高于7 m/s及更高的气速。给出了轨道长度分布和停留时间分布数据,用于分析固体在提升管内的混合。最后,将实验室规模装置收集的数据与中试规模装置收集的数据以及文献中提供的数据一起用于开发预测立管中固体速度的经验模型。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Solid phase velocity flow field and solid mixing of laboratory-scale circulating fluidized bed riser with Geldart's group B particle and scale up
A non-invasive velocity measurement technique, radioactive particle tracking, is used to measure the solid velocity flow field in a cold flow gas-solid riser at the bottom and middle sections of a laboratory scale circulating fluidized bed with Geldart's group B particles. Radial profiles of solid mean velocities, root-mean-square velocities and granular temperature are presented at various riser heights for different gas inlet velocities and solid fluxes. RPT data show that solid motion is mostly along the axial direction and mean radial motion is almost negligible. Compared to radial RMS velocity, axial RMS velocity is significantly higher. Instantaneous velocity fluctuation data show that internal recirculation is significantly higher at the gas velocities of 6 and 6.5 m/s compared to at the gas velocities of 7 m/s and higher. Trajectory length distribution and residence time distribution data presented to analyze the solid mixing in the riser. Finally, the data collected at the laboratory scale setup is used along with data collected at pilot scale setup and data available in the literature to develop an empirical model to predict the solid velocity in the riser.
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来源期刊
Chemical Engineering Journal
Chemical Engineering Journal 工程技术-工程:化工
CiteScore
21.70
自引率
9.30%
发文量
6781
审稿时长
2.4 months
期刊介绍: The Chemical Engineering Journal is an international research journal that invites contributions of original and novel fundamental research. It aims to provide an international platform for presenting original fundamental research, interpretative reviews, and discussions on new developments in chemical engineering. The journal welcomes papers that describe novel theory and its practical application, as well as those that demonstrate the transfer of techniques from other disciplines. It also welcomes reports on carefully conducted experimental work that is soundly interpreted. The main focus of the journal is on original and rigorous research results that have broad significance. The Catalysis section within the Chemical Engineering Journal focuses specifically on Experimental and Theoretical studies in the fields of heterogeneous catalysis, molecular catalysis, and biocatalysis. These studies have industrial impact on various sectors such as chemicals, energy, materials, foods, healthcare, and environmental protection.
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